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Bid Bond #2 Contract 23-19/ Venolia Water Tech PART 2
R City of Oshkosh Water Filtration Plant Ozone System Package Purchase Bid Supplement 1 - Technical Information Da;PT OF PUBTLWWORKS Table of Contents OStag OSH, 4 ISCONSIN Description Bid Section 2.1 - BIDDERS PROJECT APPROACH A Technical Proposal 1 Highlighted P&D Drawings 2 2.2 - PROCESS DESIGN CRITERIA B 2.2.1 - Ozone generation energy, oxygen, nitrogen consumption 2.2.2 - Gaseous oxygen, ozone concentration information 2.2.3 - Liquid Oxygen vaporization rates 2.2.4 - Heating requirements for gaseous oxygen supply 2.2.5 - Ozone Diffusion, Headloss, Efficiency 2.2.6 - Cooling water requirements 2.2.7 - Heat loss calculations for cooling water system 2.2.8 - Analyzer sample volume/flow requirements 2.2.9 - Safety relief valve sizing 2.2.10 - Other essential computations (if any over the above) 2.3.1, 2.3.2 - PROCESS EQUIPMENT (Data Sheets & Drawings) C Table 1 - Ozone System Package Information 1 Data Sheet Ozone Generator and Power Supply Units Dimensional layout drawings Performance Curves - 10% 03 Performance Curves - 7% 03 Complete Inverter Rating Information on HV Transformer List of specified spare parts Table 1 - Oxygen Storage and Handling Equipment 2 Data Sheet - LOX Storage Tank Dimensional layout drawings - LOX Tank Data Sheet - GOX Equipment Dimensional layout drawings - Vaporizers, Trim Heater List of specified spare parts 10/13/2023 - 10:22 AM TOC Bid Supplement 1.xls City of Oshkosh Water Filtration Plant Ozone System Package Purchase Bid Supplement 1 - Technical Information Table of Contents Description Bid Section Table 1 - Off -gas Destruct System 3 Data Sheet - Ozone Destruct Unit Dimensional layout drawing Catalyst SDS Sizing criteria for amount of catalyst Proposed approach for controlling Contact Chamber vacuum Table 1 - Cooling Water System 4 Data Sheet - Closed -loop CW system, Open -loop CW pump Dimensional layout drawing Sizing Criteria for Expansion tank, air separator, chemical pot feeder Cut -sheet, data sheet/drawing for Heat Exchanger Cut -sheet, data sheet/drawing for CW pump (O.L. and C.L.) Table 1 - Nitrogen Boost System Data Sheet - Nitrogen System Dimensional layout drawing Table 1 - Ozone Diffusion System Data Sheet - Diffusion System Layout drawing - Diffuser grid Calculation to demonstrate headloss Table 1 - Ozone System Package Instruments Cut -sheet High Cone 03 analyzer Cut -sheet Medium Cone 03 analyzer Cut -Sheet Low Cone/Ambient 03 analyzer Cut -Sheet Ambient oxygen analzyer Cut -Sheet Dew point analyzer Cut -Sheet Thermal mass flowmeter Cut -Sheet Conditionioning Orifice plate meters Cut -Sheet Electromagnetic flow meters List of specified spare parts 5 F 7 10/13/2023 - 10:22 AM TOC Bid Supplement 1.xls City of Oshkosh Water Filtration Plant Ozone System Package Purchase Bid Supplement 1 - Technical Information Table of Contents Description Bid Section 2.3.3 - ELECTRICAL DRAWINGS D One -Line Electrical Drawing 1 Bill of Materials - PLC's, OIT's, Electrical Components with ratings 2 PSU Schematic Drawing 3 2.3.4 - PROCESS AND INSTRUMENTATION DRAWINGS E P&ID Drawings - (see Chapter A - 2 above) 1 Description of I&C, P&ID (see 2.4 - Control Narrative) 2 Ozone Control Panel IMOCP, RIO1, R102 (see 2.3.3.3 - PSU Schematic Drawing) 3 Process Failures, alarms, features and SD provisions (see 2.4 - Control Narrative) 4 2.4 - GENERAL INFORMATION F System Control Narrative 1 Statement regarding anticipated fluctuation in electrical power including peak draws during startup 2 List of all monitored process conditions and location, condition and range of each 3 2.5 - PROJECT AND IMPLEMENTATION SCHEDULE G 2.5.1 - Preliminary Project Schdule 1 2.5.2 - Table of Site Times 2 10/13/2023 - 10:22 AM TOC Bid Supplement 1.xls October 13, 2023 To: City of Oshkosh Room 310 of City Hall 215 Church Avenue Oshkosh, WI Re: City of Oshkosh Water Filtration Plant Ozone System Package City of Oshkosh, WI Purchase Project No. 8679292 Ozone System — Specification Sections 44 44 56S, 44 44 56.01 S, 44 44 56.02S, 44 44 56.03S, 44 44 56.05S, 44 44 56.07S, 44 44 56.08S, 44 44 56.11S, 40 99 9 1 A and related sections regarding piping, instruments, valves, mechanical and electrical and Oshkosh (as part of the Bid Documents) Ozone Drawings Proposal No. 533310 To Whom it May Concern: Veolia Water Technologies Treatment Solutions USA, Inc. (formally SUEZ Treatment Solutions, Inc.) is the first -named supplier for the ozone generation system equipment and services for the above project. The specifications and drawings have been developed around Veolia's equipment and we are very experienced working with the Consulting Engineer on previous projects. Veolia Water Technologies Treatment Solutions USA, Inc. (hereafter Veolia) is the largest Ozone Systems Supplier in North America today with over 135 operatingapgLating Municipal Water installations in North America totaling over 350,000 Ibs/day of ozone generating capacity. Veolia shall provide the following equipment and services in full compliance with specification sections 44 44 56S, 44 44 56.01 S, 44 44 56.02S, 44 44 56.03S, 44 44 56.05S, 44 44 56.07S, 44 44 56.08S, 44 44 56.11S, 40 99 91A and related sections regarding piping, instruments, valves, mechanical and electrical and Oshkosh Ozone Drawings (as part of the Bid Documents). This proposal includes any modifications from Addendum nos. 1 — 4. If you have any questions, or require more information, please do not hesitate to contact our representative, whose address is listed below, or the undersigned. Note: Any changes made in Rev. 1 of the proposal are shown as bold italics for changes or additions, and stl4lethfGW948 for deletions. Very truly yours, Veolia Water Technologies — Treatment Solutions USA, Inc. William Nezgod Senior Sales Manager — Engineered Ozone Plants Proposal 533310_Oshkosh FINAL_10-13-23.Docx 1 of 23 Proposal and Contract TO: City of Oshkosh Proposal No.: 533310 Room 310 of City Hall 215 Church Avenue Date: October 13, 2023 Oshkosh, WI For: City of Oshkosh Water Filtration Plant Ozone System Package Purchase City of Oshkosh, WI Project No. 8679292 (Hereinafter referred to as "Purchaser") Veolia Water Technologies — Treatment Solutions USA, Inc. (hereinafter referred to as "Veolia") offers to furnish the following described materials and equipment ("Products") and/or services at the prices ("Purchase Price") stated herein. This Proposal shall remain in effect for from the date hereof and shall expire at that time unless extended in writing by Veolia. This Proposal and any resulting contract shall be referred to hereinafter as "this Contract". Sections 44 44 oca `— - v --w -- 56.05S 44 44 56.07S 44 44 56.08S 44 44 56.11 S 40 99 91 A and related sections re ardi I Ing i in instruments valves mechanical and electrical Drawings: P&ID's 008-N-001 to 008-N-014, 008-N-021, 022 The above to be provided as described herein. Sales Representative: William/Reid Mr. Brandon Mancilla Tel: 414-331-5576 Email: brandon@williamreidltd.com Reaional Manager Veolia Technologies and Solutions Mr, John Hughes Email: john.hughes1@veolia.com Proposal 533310—Oshkosh FINAL-10-13-23.Docx 2 of 23 A I. SCOPE OF SUPPLY I. LOX/GOX Equipment 2. Ozone Generator/PSU System 3. Closed Loop Cooling Water System 4. Supplemental Nitrogen System 5. Ozone Diffusion System 6. Ozone Destruct System 7. Ozone Master Control Panel 8. Ozone, Oxygen & Dewpt. Monitors 9. Field Instrumentation 10. Misc. Equipment and Services 11. Spare Parts and Misc. Equipment 12. Coordination Meetings 13. Field Service, Testing and Training Optional Equipment 1. None at this time II. EQUIPMENT AND SERVICES DESCRIPTION 2 x 9,000 gallon Horizontal LOX tanks 1 x CGA Hose connection fitting 3 x 120 SCFM Ambient Vaporizers 2 x Trim Heaters 2 x Gaseous Oxygen (GOX) Filters 2 x GOX Pressure Regulators 3 x 600 ppd @ 10% 03 3 x Closed -loop CW Skids 3 x Open -loop CW pumps w/instr. & valves 1 x 100% capacity unit 4 x Sets of Diffuser drop piping, manifold piping 1 x Lot Diffusers 1 x Lot of Field Instruments and Valves 2 x Demisters 3 x Ozone Destruct skids 1 x Master Ozone Control Panel 1 x RIO-D2 at LOX Area 1 x RIO-DI at Contactor Gallery Area 1 lot as described below 1 lot as described below 1 lot as described below 1 lot as described below 1 lot as described below 1 lot as described below A. LOX / GOX Equipment: Section 44 44 56 and Drawings 008-N-001 Veolia shall provide the following equipment in accordance with the above specification and as shown on highlighted P&ID drawing 008-N-001, 008-N-003 • Two (2) 9000 gallon horizontal Liquid Oxygen (LOX) Storage tanks (T4007-1, T4007-2) including required instrumentation and valves as specified. • Two (2) 1.5 in Liquid Oxygen CGA hose connection fitting with integral mounting bracket and cap for the LOX tank fill piping Proposal 533310_Oshkosh FINAL_10-13-23.Docx 3 of 23 One (1) Remote Truck Fill Stand with 316 SS piping and valves and 1-1/2" CL 300 304SS Flange connection Three (3) Thermax model SG140HF Ambient Vaporizers (M4en7GOX) oThis equates to 120% capable of handling 120 SCFM (7200 SCFH) of gaseous oxygen of the max. gas flow in summer at a 12 hr cycle and 60 SCFM in the winter at an 8 hr cycle. (per Addendum no. 2) One (1) Vaporizer Switching Skid to include the following: o 1-1/2" 3-Way Switching skid with 316 SS Piping and Valves o 3 x Electric Actuated ball valves o 3 x ASME rated pressure relief valves o 3 x Temperature switches o 1 x Temperature Transmitter (TIT) • Two (2) Thermax model TBT9 Trim Heaters (M4027-1, M4027-2) • One (1) Liquid Oxygen Unloading Panel (LCP4004) as shown in highlighted P&ID 008-N-001 • Two (2) Pipe spools before the Trim Heater, each to include the following o One (1) Isolation Ball valve o One (1) Flanged 316L SS pipe spool to include the above equipment. Two (2) Pipe spools after the Trim Heaters, each to include the following: o One (1) Low temperature shutoff valve o One (1) Ball valve o One (1) Flanged 316L SS pipe spool to include the above equipment. The following Instruments and Valves shall be shipped loose to be installed in the field by the Contractor: XXX) i T� 4030-A) OX line after the Trim Heaters o One (1) Pressure Relief Valve (PRV-X o One (1) Temperature Indicating Transmitter o One (1) Temperature Switch, Low (TSL-4030-B) o Two (2) Orifice Plate Flow Elements (FE-4032-1, FE-4032-2) o Two (2) DP Flow Indicators (FI-4032-1, FI-4032-2) o Two (2) Pressure Indicators (PI-4033-1, PI-4033-2) o Two (2) Pressure Indicating Transmitters (PIT-4033-1 B, PIT-4033-2B) o Two (2) Pressure Relief Valves (PRV-XXXX, PRV-XXXX) o Two (2) Emergency Shutoff Valves (FV-4035-1, FV-4035-2) Chart shall provide the following Insulated Piping (Between Tanks and Vaporizers): • o (36 ft) 1-1/2" x 3-1/2" rigid VIP (Vacuum Jacketed Piping) o (8ft) 2" ID x 4" OD Flex (4 locations) o Internal Bellows Design o 250 psig MAWP o DV6 Vacuum Tester at Each Section 4 of 23 Proposal 533310_0shkosh FINAL_10-13-23.Docx • Type 316L SS field piping between outlet of Vaporizer Switching skid and the inlet Pipe spoof to the Electric Trim Heaters. The 2-1/21, or 3" pipe spools shall provided flanged and cleaned for oxygen service. Note: Field cleaning of the GOX piping shall not be necessary and if required by Engineer shall be at the Cost of the Installing Contractor. • Chart shall provide the design of the LOX piping between the LOX tanks and Vaporizers and field piping between the Vaporizer switching skid and Trim Heaters. B. Gaseous Oxygen Equipment: Section 44 44 56, 44 44 56.02 and Drawing 008-N-003 Veolia shall provide the following equipment, instruments and valve as shown in highlighted P&ID drawing 008-N-003: 1. One (1) GOX Particle Filter/Pressure Regulating Assembly including the following equipment, instruments and valves per the highlighted P&ID (008-N-003): o Two (2) Graver Consler Particulate Filters (M4039-1, M4039-2) o Two (2) Pressure Differential Indicators around the GOX filters (PDI-4039-1, PDI-4039-2) o Two (2) Cashco model SL-2 Pilot Operated Pressure Regulating Valves (PCV-4043-1), PCV-4043-2) designed to handle the full range of gas flow from 60 — 1440 Ibs/day of ozone at 10% 03 concentration (design is 120% of rated gas flow) o Three (3) Pressure Relief valves o Six (6) Ball valves before the Pressure Regulators o Two (2) Butterfly valves after the pressure regulator o One (1) piping assembly per the highlighted P&ID drawing 2. One (1) Gaseous Oxygen Monitory Assembly to include the following frame mounted components: • Two (2) manual isolation Butterfly valves (FV-4045-1, FV-4045-2) • Four (4) Dew point analyzers (AIT-4048-1, AIT-4048-2, AIT-4051-1, AIT-4051-2) • Two (2) Temperature Indicating Transmitters (TIT-4049-1, TIT-4049-2) • Two (2) Thermal Mass Flow Transmitters (FIT-4052-1, FIT-4052-2) • Three (3) Isolation Ball valves to confirm the flow rate from the FIT's • One (1) Orifice Plate and DP flow Indicator to measure the GOX gas flow rate 3. Manual Isolation Field Valves • Three (2) Manual Isolation Ball Valves (FV-4036-1, FV-4036-2, FV-4036-3) • Four (4) Manual Isolation Butterfly Valves (FV-4056-1, FV-4056-2, FV-4056-3, FV-4056-4) to be shipped loose for installation in the field C. LOX-GOX Piping Design As requested in the specifications, Veolia will provide the design for the piping of the Vacuum Jacked LOX piping between the LOX tanks and Vaporizers. We will also provide a preliminary design for the GOX piping between Vaporizers and Electric Trim Heaters. Proposal 533310_Oshkosh FINAL_10-13-23.Docx 5 of 23 Note: The design of field piping is not part of the standard design and Electrip Tr imeHeater) oaeither Veol a Chart (supplier of LOX tank, Vaporizer, Vacuum Jacketed piping I and fit up in the site where it is (Ozone System Supplier) as there is field piping design, supp y the customary for the Contractor to take on thisdinsps me Ilnstallatlity as honOSupery s on sere cesSS is not on site rb t this installation process. The OSS may be providingcope of work be does not entail an extended site presence. It is recommended a ed t pat thence to minimize installation by the Engineer/Contractor as both parties will b g delays. We will provide a deduct (see options) to remove this service that is best handled by other parties. D. Ozone Generators: Section 44 44 56, 44 44 56.01, Highlighted Drawing 008-N-007 and Veolia shall provide the following equipment in accordance with the above specification sections as shown on highlighted P&ID drawing 008-N-007: Three (3) Veolia Model Ozonia SP-73 Advanced Technology 'IGS' skid -mounted medium frequency Ozone Generators (M4120-2, M4120-3, M4120-4), each it capable of feed (LOX) gas with cooling ay of ozone at a concentration of 10% by weight from a liquid oxygen water temperature of up to 86 "F. The ozone generators lprovided riped for ease ofinstallation. shall include the following instrumentation and valves, pre -wired lied as a complete assembly for ease of The ozone generator vessel and pipe skid shall be supplied installation. Model SP-73 Ozone Generator Skid w1power supply 6 of 23 Proposal 533310_Oshkosh FINAL_10-13-23.Docx The ozone generator skid shall include the following instrumentation and valves for the ozone generator and power supply unit: Instrumentation oty. Tag No. (on Gen 2) Oxygen Inlet Line 1 PIT-4113-2 1 FIT-4114-2 Manufacturer Endress & Hauser Kurz or Endress & Hauser 1 PI-4115-2 Ashcroft 1 PSH-4115-2 Ashcroft PSL-4116-2 1 TIT-4118-2 Endress & Hauser Cooling Water Inlet Line 1 PI-4242-2 Ashcroft 1 TIT-4234-2 Endress & Hauser Ozone Outlet Line 1 TSH-4121-2 Ashcroft 1 TIT-4122-2 Endress & Hauser 1 PI-4123-2 Ashcroft 1 AIT-4130-1 Teledyne 465-H Cooling Water Outlet Line 1 TSH-4246-2 Ashcroft 1 PI-4247-2 Ashcroft 1 TIT-4246-213 Endress & Hauser 1 FIT-4248-2 Endress & Hauser 1 FI-4255-2 King Inst or equal 1 TIT-4256-2 Endress & Hauser Valves Instrument Description Pressure Indicating Transmitter Flow Indicating Transmitter Pressure Indicator Pressure Switch — High/Low Temperature Transmitter Pressure Indicator Temperature Indicating Transmitter Temperature Switch Temperature Indicating Transmitter Pressure Indicator High Concentration Ozone Analyzer Temperature Switch — High Pressure Indicator Temperature Indicating Transmitter Flow Indicating Transmitter Flow Indicator (PSU) Tem�peratu�relndi�catingTransmitter Proposal 533310—Oshkosh FINAL_10-13-23.Docx 7 of 23 .,� Tan�No.ManufacturerValve .. gOxygen Description��y, Inlet Line FV-4111-2 Sharpe or Apollo Manual isolation Valve 1 1 FV-4112-2 Sharpe or Apollo Motorized Isolation Valve 1 FV-4119-2 Check All or equal Check Valve 1 PRV-XXXX-2 Kunkle Safety Relief Valve (Gas) Ozone/Oxygen Outlet Line 1 FV-4124-2 Sharpe or Apollo Motorized Isolation Valve 1 FV-4125-2 Check All or equal Check Valve 1 FV-4126-2 Sharpe or Apollo Manual Isolation Valve 1 BV-XXXX Sharpe or Apollo Purge Manual Isolation Valve 1 FV-4561-2 Sharpe or Apollo Motorized Purge Isolation Valve 1 FV-4562-2 Globe Valve Cooling Water Inlet Line (Closed -Loop) 1 FV-4240-2 Bray or Flowseal Manual Isolation Valve 1 FV-4241-2 Bray or Flowseal Motorized Shut Off Valve 1 FV-4244-2 Bray or Flowseal Manual Isolation Valve Pressure Relief Valve (Thermal) 1 PRV-XXX Kunkle 1 FV-4245-2 Sharpe or Apollo Drain Valve Sharpe or Apollo Manual Isolation Valve (PSU supply) 1 FV-4250-2 Cooling Water Outlet Line (Closed -Loop) 1 BV-XXXX Sharpe or Apollo Manual Isolation Valve Air Release Valve (high point) 1 ARV-XXX 1 FV-4249-2 Check Valve Isolation Valve (PSU return) 1 FV-4250-2 Sharpe or Apollo Manual Check Valve (PSU return) 1 FV-4257-2 FV-4258-2 Bray or Flowseal Manual Isolation Valve Note: The Base Design has the Ozone Generator and Power Supply unit mounted on the same skid, resulting in a fully wired deliverable. If determined, to or logistic arate the Ozone Generatoon to move � the and Power reas equipment room, that it would be SupplyUnits could be designed such that they Supply Unit, the Ozone Generator and Powersign would be shipped separately. In that case, the signals and controls wiring would be wired from xes on the generator skid. Once tio the generator instruments and devices to local junc it areoset in place in the field, the contractorboth the ozone generator and the Power Supply would then install the required conduits and pull all the wiring from the junction boxes to the Proposal 533310_Oshkosh FINAL_10-13-23.Docx A Power Supply Unit. Similarly, the contractor would also be required to install the necessary conduits for the High Voltage cables, and pull those cables, which are provided by Veolia, from the PSU to the ozone generator. Termination of the High Voltage (HV) cable would then be accomplished by Veolia staff. E. Power Supply Units: Section 44 44 66.01, Highlighted Drawing 008-N-007 Veolia shall provide the following equipment in accordance with the above specification sections and as shown on highlighted P&ID drawing 008-N-007. Three (3) Veolia Model Ozonia IPS-16-0200-WC-12 Medium Frequency Power Supply Units (M4130- 2, M4130-3, M41303). These PSU's utilize the latest in IGBT (Insulated Gate Bipolar Transistor inverter technology. The PSU will be controlled by a Schneider Electric standalone M580 PLC with Schneider Electric Harmony GTO operator interface terminal (OIT). The electrical enclosure shall be a NEMA 12 painted steel enclosure. The PSU shall be located on a separate skid from the ozone generator vessel. Note: PLC code & logic control functions, as well as GIP graphics & symbols, shall be programmed based on Veolia standards The following are some of the advantages of the IGBT Converter/Inverter based Power Supply Unit over the older SCR (Silicon Controlled Rectifier) based technology: • Power supply operates at almost unit Power 0.97) over the • Power supply unit has a power turnd wn up to 100r 1 to he ozone a erator operating range • Low operating voltage < 4000 volts g essel • Power supply exhibits very low harmonics, below the latest requirement of IEEE519 • Power Supply uses and "active front-end" IGBT based Converter design and constant frequency inverter switching at whole multiples of the line frequency. • Line notching that is typical of SCR's and diode based converters is also eliminated • Designed to meet electrical arc flash requirements • Designed to meet the latest CA fire codes Three (3) sets of HV cables to be installed in the field by the Contractor if the Ozone Generator and Power Supply skids are shipped separately. Veolia will terminate the cables in the field prior to commissioning. Note: If the 03 Generator and Power Supply unit are shipped on the same skid, Veolia will supply and wire the HV cable between the 03 Generator and PSU. F. Nitrogen Boost System — Specification 44 44 56.03, Highlighted dwg. 008-N-003 Veolia shall provide one (1) skid -mounted Nitrogen boost system including the following equipment components in accordance with the above specification section and as shown on highlighted P&ID drawing 008-N-003: Duplex oil -free rotary scroll compressors (M4902-1, M4902-2) Air-cooled aftercoolers Proposal 533310—Oshkosh FINAL_10-13-23.Docx 9 of 23 re -I -TV r W • One (1) Air receiver tank (T4905) • Two (2) Coalescing pre -filters (M4911-1, M4911-2) • Two (2) Heatless dual tower desiccant dryers (M4912-1, M4912-2) • Two (2) Particulate filters after the dryers (M4913-1, M4913-2) • One (1) Pressure regulating valve (PCV-4916) • One (1) Mass flow controller (FIT-4920-1/FCV-4922-1) • One (1) Flow Indicator (FI-4920-2) • One (1) lot required instrumentation • One (1) lot manual isolation valves • One (1) check valve • One (1) Local control panel (LCP-4902) • One (1) Power Panel (*PP-4902) (*Veolia Standard) G. Open -Loop and Closed Loop Cooling Water System: Sections 44 44 56.08 and Highlighted Drawings 008-N-004, 008-N-005, 008-N-006 Veolia shall provide a open -loop and closed -loop cooling water system in accordance with the above specification sections and highlighted drawings 008-N-004, 008-N-005, 008-N-006, consisting of the following major components shipped loose for installation in the field by the Contractor: 1. Open -Loop Cooling Water Skid Dwg 008-N-004 Three (3) Open -loop Cooling Water Skids as per highlighted P&ID 008-N-004, each skid including the following (tag nos. are for skid no. 1): • One (1) Goulds, Aurora or equal 5 hp Open -loop Cooling Water pumps (P4263-1) — The pump shall provide up to 90 gpm of open -loop cooling water to the closed -loop CW skid at a pressure of — 75 ft TDH • Two (2) Manual Isolation Butterly Valves (FV-4261-1, FV-4266-1) located before and after the pump. • Two (2) Pressure Indicators (PI-4262-1, PI-4265-1) located before and after the pump • One (1) Check Valve (FV-4264-1) after the pump. • Skid -mounting including piping to skid edge limit. 2. Field Cooling Water Equipment— Highlighted Drawing 008-N-005 Veolia shall provide the following closed -loop cooling water components, shipped loose for installation in the field by the Contractor: • One (1) Air Separator (M4200) • Two (2) Isolation ball valves • One (1) Air release valve • One (1) Chemical Pot Feeder (M4205) • Two (2) Isolation valves (FV-4206, FV-4207) • Two (2) Sample valves Proposal 533310_Oshkosh FINAL_10-13-23.Docx 10 of 23 One (1) Expansion Tank (T4210) Two (2) Isolation ball valves (FV-4211, FV-4212) One (1) Closed -loop CW Supply Fill connection with required valves 3. Closed -loop Cooling Water Skids — Section 44 44 66.08, Highlighted Dwg. 008-N-006 In accordance with the above specification and highlighted P&ID drawing 008-N-006, Veolia shall provide the following closed -loop Cooling Water System equipment (M4220-2, M4220-3, M4220-4), including the following instruments and valves. The CW system shall include the following major components (tag nos. are for unit no. 2): Equipment Qty. Tag No. Manufacturer Instrument Description Equipment 1 M-4230-2 Polaris Plate and Frame Heat Exchanger 1 P4225-2 Goulds, Aurora, Grundfos or equal 5 hp End -suction centrifugal pump 1 M4223-2 Strainer 2 JB-XXXX J B-XXXX Junction Boxes for skid signals Instruments Qty. I Tag No. Manufacturer Instrument Description Instruments — Open -loop CW line 1 FIT-4271-2 Endress & Hauser Flow Indicating Transmitter 1 PIT-4273-2 Endress & Hauser Pressure Indicating Transmitter 1 TI-4275-2 Ashcroft or equal Temperature Indicator 1 PDIT-4230-2B Differential Pressure Transmitter around open -loop side of H/E 1 PI-4276-2 Ashcroft Pressure Indicator 1 TI-4277-1 Ashcroft Temperature Indicator Instruments — Closed -loop Chilled Water line 2 PI-4224-2 PI-4232-2 Ashcroft Pressure Indicator 2 TI-4228-2 TI-4233-2 Ashcroft Temperature Indicator Proposal 533310_Oshkosh FINAL_10-13-23.Docx 11 of 23 Instrument Description Tag No. Manufacturer Pressure Indicating Transmitter PIT-4227-2 n Endress & Hauser Valves Valve Description Qty, Tag No. Manufacturer Open -Loop CW Line Manual Isolation Butterfly Valve 1 FV-4270-2 Bray, Flowseal, or Henry Pratt Motorized Isolation Butterfly Valve 1 FV-4272-2 Bray, Flowseal, or Henry Pratt FV-4278-2 Bray, Flowseal, or Manual Isolation Butterfly Valve 1 Henry Pratt Closed -Loop CW Line Manual Isolation Butterfly Valve 1 FV-4221-2 Bray, Flowseal, or Henry Pratt Motorized Isolation Butterfly Valve 1 FV-4222-2 Bray, Flowseal, or Henry Pratt Check Valve 1 FV-4226-2 Pressure Relief Valve 1 PRV-XX XX Kunkle (PRV is not required) FV-4234-2 Bray, Flowseal, or Manual Isolation Butterfly Valve 1 Henry Pratt 008-N-08, -009 H. Diffusion System Equipment: Section 44 44 66.05 and Highlighted Dwg. following diffusion In accordance with specification section 44 44 56.05, Veolia shall provide the fo 9 equipment: • Four (4) sets of type 316E SS drop piping • Four (4) Diffuser manifolds and heater ring as chalmbe s th rough he portholes requiredies, designed with the ant e flanges of access the diffusion area of the existing contact the chambers. 128 ozonic® 7 in diameter porous ceramiadiffusers eofheach manifospecifications ld May be reduced to Up to 16 blow -off diffusers to be located the bottom two per diffuser ring during detailed design. The following are field instruments and field valves to be provided loose for installation in the field by the Contractor: 12 of 23 Proposal 533310_Oshkosh FINAL 10-13-23.Docx A Instruments QtY. Tag No. Manufacturer Instruments — Ozone to Diffusion System 2 FIT-4305-1 Kurz or Endress & FIT-4305-2 Hauser 2 PIT-4305-1 Endress & Hauser PIT-4305-2 2 TIT-4305-1 Endress & Hauser TIT-4305-2 4 PIT-4315-1 Endress & Hauser PIT-4315-2 PIT-4325-1 PIT-4325-2 4 FIT-4315-1 FIT-4315-2 Kurz or Endress FIT-4325-1 Hauser FIT-4325-2 Valves Qty. Tag No. Manufacturer Valves — Ozone to Diffusion System 2 FV-4304-1 FV-4304-2 Bray, Flowseal, or equal 2 FCV-4305-1 Sharpe or Worcester FCV-4305-2 4 FCV-4310-1 Sharpe or Worcester FCV-4310-2 FCV-4320-1 FCV-4320-2 Instrument Description Flow Indicating Transmitter in the main 03 line to Contact Chambers Pressure Indicating Transmitter in the main 03 line to Contact Chambers Temperature Indicating Transmitter in the main 03 line to Contact Chambers Pressure Indicating Transmitter in the 03 delivery lines to Diffusion Cells & IFlow Indicating Transmitter in the 03 delivery lines to Diffusion Cells Valve Description Manual Isolation Butterfly Valve in main 03 line to Contact Chambers Motorized V-port flow control valve in main 03 line to Contact Chambers Motorized V-port flow control valve in 03 delivery lines to Diffusion Cells I. Ozone Destruct System; Section 44 44 66.07 and Highlighted Drawings 008N 008-N- 009, 008-N-12--008 Veolia shall provide the following equipment in accordance with the above specification section a shown on highlighted P&ID drawings 008-N-008, 008-N-009 and 008-N-012: nd as 1- Ozone Destruct Skids Three (3) Veolia model Ozonia Size 2 Thermal/Catalytic ozone destruct units (M4500-1 M45 - M4500-3), each unit capable of handling up to 66 SUM of chamber off -gas flow and reducin 00 2, ozone concentration to < 0.08 ppm by volume. g the Proposal 533310_Oshkosh FINAL_10-13-23.Docx 13 of 23 A Each ozone destruct unit shall be a skid -mounted unit consisting of the following major components (tag nos. are for M4500-1): • One (1) Manual isolation butterfly valve (FV-4510-1) • One (1) Motorized isolation butterfly valve (FV-4511-1) • One (1) Make-up air filter • One (1) Motorized air inlet valve (FV-4513-1) • One (1) Orifice plate (FI-4513-1) • One (1) Manual isolation ball valve • One (1) Check valve (FV-4515-1) • Three (3) Temperature elements/transmitters (TE/TIT-45• 19-1,TE/TIT-4523-1, TE/TIT-4531-1) One (1) pre -heater with SCR based control (M4520-1) • One (1) Temperature switch 0-1) with Pressure differential indicating transmitter • One (1) 316L SS catalyst chamber (M453 (PDIT-4530-1) One (1) Vent gas Ozone Analyzer (AIT-4550-1) in the vent line after the blower •• One (1) Cincinnati Fan or NY Blower 2 or 3 hp Off -gas Blower with Pressure differential transmitter (PDIT-4540-1) • One (1) Pressure Indicating Transmitter (P• IT-4541-1) One (1) Check Valve (FV-4542-1) after the blower • One (1) Manual isolation valve (FV-4543-1) • One (1) Silencer (M4544-1) (shipped separately for field mounting) • One (1) lot interconnecting piping and wiring to provide for a complete skid -mounted unit • One (1) lot instrumentation and valves as shown on P&ID drawing • Drain valves as required anel (LCP4501-x) located on the destruct skid in a • One (1) Ozone Destruct Local Control P NEMA 4X enclosure One (1) Ozone Destruct Power Panel (LCP4502-x) located on the destruct skid in a NEMA 4X •enclosure 14 of 23 Proposal 533310_Oshkosh FINAL_10-13-23.Docx Ozone Destruct Skid 2. Field Equipment, Instruments and Valves — Highlighted Drawing 008-N-008, .009 Veolia shall provide the following equipment, instruments and valves, shipped loose for installation in the field by the Contractor: • Two (2) Pressure (Vacuum) Indicating Transmitters (PIT-4330-1, PIT-4330-2) in the Off -gas line from the Contact Chambers • Two (2) Demisters (M4331-1, M4331-2) in the Off -gas line from the Contact Chambers • Two (2) Differential Pressure Transmitters (DPIT-4331-1, DPIT-4331-2) around the demisters • Two (2) Vacuum/Pressure relief valves in the Off -gas line from the Contact Chambers • Two (2) Manual Isolation Butterfly Valves (FV-4332-1, FV-4332-2) in the Off -gas line from the Contact Chambers. J. Ozone System Control Panels (not located on equipment skids): Section 13290, Drawings 21- 1,4,5, 31-1,3,4,5, 41-1, 91-2, and GI-31 Veolia shall provide field mounted control panels in accordance with the above specification section and as shown on highlighted P&ID drawings referenced above: 1. Master Ozone Control Panel (CP-PLC-D, aka MOCP) One (1) Master Ozone Control Panel (CP-PLC-D) to include redundant Schneider Electric M580 PLC processors to monitor and control the entire ozone system as described section 44 44 56 of the specifications and as shown on the P&ID's and Control System Architecture drawing 008-N- Proposal 533310_Oshkosh FINAL 10-13-23.Docx 15 of 23 A 002. The MOCP shall include a Schneider Electric 15-inch color touchscreen OIT to provide operation screens. 2. LOX Remote IIO Control Panel (CP-RIO-D2) l the One (1) LOX Remote 1/0 Control Panel to collect instruments and valves as shown on drawing 008 N!001. sTelemetry shall be transmitted ignals from the LOX ovequer fiber optic communication link to and from Master Ozone Control Panel (CP-PLC-D). 3. Ozone Gallery Remote 110 Panel (CP-RIO-Di) als One (1) Contactor Gallery Remote 1/0 Control Panel ntell to collect all the sign ety systermminstrumentsothe land cooling water pumps, contactors, destruct units, gallery asedlocation valves as shown on multiple P&ID pages. Bansm tted over fiber panel optic link tlo be NEMA 4X Stainless Steel. Telemetry shall be tr and from Master Ozone Control Panel (CP-PLC-D). K. Field Located Ozone and Oxygen Gas Phase Monitoring Equipment: Section 44 44 56, 40 99 91A Drawings 008-N-008, -009, -013, and 008-NO-014: and oxygen monitoring equipment shall be provided: The following gas phase ozone Instrumentation Shipped Instrument Description Qty P&IRef Tag No. Mfg. Part or Dew point Analyzer 4 008-N-003 AIT-4048-1 AIT-4048-2 Michell met II ( ) GOX AIT-4051-1 Assembly AIT-4051-2 On Gen High Concentration Ozone 3 008-N-007 AIT-4130-2 Teledyne le Skid Analyzer (On gen skid) AIT-4130-3 AIT-4130-3 Shipped Medium Concentration Off - 2 008-N-008 AIT-4340-1 Teledyne 465M Loose gas ozone analyzer 008-N-009 AIT-4340-2 Vent Gas Ozone Analyzer 3 008-N-012 AIT-4550-1 Teledyne 465L On Destruct AIT-4550-2 Skid AIT-4550-3 Shipped Ambient Ozone Analyzer 4 008-N-012 AIT4605-1 AIT4605-2 Teledyne 465E Loose 008-N-013 AIT-4610-1 AIT-4610-2 16 of 23 Proposal 533310_Oshkosh FINAL 10-13-23.Docx A QtY I P&ID Ref Tag No. Mfg. 4 008-N-012 g Shipped Instrument Description AIT4615-1 Teledyne Shipped Ambient Oxygen Analyzer 008-N-013 AIT4615-2 3340 or Loose AIT-4620-1 MSA Ultima X AIT-4620-2 Specification Section 44 44 66 • One (1) Aeroqual Portable ozone leak monitor as per 1.06.E.9 of specification section 44 40 99 91A L. Miscellaneous Field Equipment: Highlighted Drawings 008-N-001, In accordance with P&ID drawing 21-1 Veolia (SUEZ Treatment Solutions) shall provide the following field mounted instrumentation: • One (1) Temperature Indicating Transmitter (AIT-4300) to measure ambient outside temperature in the LOX area • One (1) E-Stop switch in LOX/Vaporizer Area (HS-4665) • Seven (7) E-Stop switch (HS-4635-D, HS-4635-E, HS-4635-F, HS-4635-G, HS-4640-D, HS- 4640-E, HS-4640-F) near identified equipment areas or doors M. Spare Parts Veolia (SUEZ Treatment Solutions) shall provide the following spare parts in accordance with section 44 44 56.01, 44 44 56.03, 44 44 56.05, 44 44 56.07 and 44 44 56.08. Spare parts as specified in paragraph 1.07 of section 44 44 56 • Two (2) Spare oxygen filter elements • Spare parts for all gas phase ozone analyzers • Spare service kit for each oxygen analyzer 2. Spare parts as specified in paragraph 1.07 of section 44 44 56.01 including the following: • 5% of dielectrics for one ozone generator • Six (6) sets of ozone generator head gaskets • 10% of fuses for one ozone generator • One (1) complete set of PSU fuses • One (2) sets of complete circuit board replacement for a PSU • Two (2) glass viewports and gaskets for one ozone generator • One (1) set of special tools for ozone generator maintenance • One (1) wet test meter and dewpoint cup for testing (to remain with Owner) • Zero (0) Air filters for PSU (Not applicable — Veolia PSU's do not utilize internal air filters) 3. Spare parts as specified in paragraph 2.06 of section 44 44 56.03 including the following: Proposal 533310 Oshkosh FINAL_10-13-23.Docx 17 of 23 e • One (1) set of V-belts for compressor • Two (2) Intake Filter cartridges • One (1) set of spare desiccant dryer towers • Two (2) sets of coalescing filter elements • Two (2) sets of particulate filter elements • One (1) set of fuses for N2 local control panel 4. Spare parts as specified in paragraph 1.07 of section 44 44 56.07 including the following: One (1) complete set of gaskets for one destruct unit One (1) pre -heater elements for the ozone destruct One (1) full vessel catalyst charge for one off -gas destruct unit One (1) Demister mesh replacement Three (3) sets of line power fuses th 5. Spare parts as specified in paragraph 1.05 of section 4444 56, inclu d ng ffusee gaskets 32 x spare Garlock Gylon 3545 PTFE or equal (per mfg.standard) 32 x spare regular ozone diffusers 2 x spare blow -off diffusers with mounting bolts 6. Spare parts as specified in paragraph 1.09 of section 44 44 56.08 including the following: Two (2) sets of bearing kits for an open -loop cooling water pump Two (2) sets of closed -loop cooling water pump bearing kits Three (3) gaskets for heat exchangers 7. Control System Spare Parts (section 40 99 91) including the following One (1) of each type and size of OIT used One (1) of each type and size of Controller Processor used. One (1) of each type and size of Controller Chassis used. One (1) of each type and size of Controller Power Supply used. One (1) of each type and size of Controller Communication Module used. One (1) of each type and size of PLC 1/0 Module used. One (2) of each type and size of Controller Field Potential Distribution Modules used. One (1) of each type of Ethernet Switch. Twenty (20) percent of each type and size of DC Power Supply used, not less than 1. Twenty (20) percent of each type and size of Fuse used, not less than 5. Twenty (20) percent of each type and size of Control Relay used, not less than 3. Ten (10) percent of each type and size of Terminal Block used, not less than 10. Ten (10) percent of each type and size of Intrinsic Safety Barrier used, not less than 1. Ten (10) percent of each type and size of Pilot Light used, not less than 1. Ten (10) percent of each type and size of Hand Switch used, not less than 118 of 23 Proposal 533310_oshkosh FINAL_10-13-23.Docx ROM L. Miscellaneous Equipment and Services Veolia shall provide the following Miscellaneous Equipment and Services: • Seismic calculations as required for individual equipment specification sections to determine the size and location of the anchor bolts for equipment or equipment skids. M. Engineering and Coordination Provided Veolia will provide the following Engineering information in accordance with the issued specifications. Veolia will provide all necessary design, installation and operating information for equipment provided by Veolia. Veolia will coordinate and review other equipment items associated with the ozone system but will not be responsible for the design, installation and operation of equipment and systems supplied by others. Design Coordination Meetings In accordance with Par. 1.06.B of specification section 44 44 56.11, Veolia shall provide the following Engineering Coordination meetings/support: g • Ten (10) Virtual Design Coordination meetings • Coordination meetings on screen layouts, Process Control Narrative and testing requirements Pe par. 3.05 of section 40 99 91 Engineering Information Provided 1. System Integration Engineering 2. General equipment orientation and dimensional drawings components. for all equipment and system 3. Process and Instrumentation drawings (P&ID) for each piece of equipment. 4. Electrical schematics, panel layouts and interconnecting terminal block drawings for all controls and instruments supplied. 5. Office and field coordination with the Contractor and I&C subcontractor. 6. Equipment layout and data including manufacturer, model, power requirements, capacity and materials of construction. 7. Storage, handling and erection requirements. 8. Foundation loading and anchor bolt calculations. 9. Performance test procedures. 10. Operations and Maintenance manuals N. Factory Testing Veolia shall include the required Factory Acceptance Testing (FAT) in accordance with par. 3.02 of section 13290. Tests shall include cause and effect testing, ozone production testing. Testing may be witnessed by Engineer (Construction Manager) at their own expense. Proposal 533310_Oshkosh FINAL_10-13-23.Docx 19 of 23 A O. Services — Installation Supervision, Commissioning, Testing and Training Veolia shall provide the following commissioning, testing and training services in accordance with par. 3.02 of specification section 13290 including the following: 1. Phase 1: Inspection and Commissioning Ten (10) person -days for installation assistanDestruct,cCWlSystem,nMOCP,kAnalyzers a out and pre - commissioning of 03 Gen/PSU, ozone Nitrogen Boost system for functional a Ada Operational Readiness Testing for O Twenty (20) person -days se I Generation system equipment that is part of p Five (5) person -days for LOX-GOX System installation assistance, inspection and checkout of Manufacturer Proper Installation Five (5) person -days for functional and operation read Five on assistance, ting for the nspection a d Five (5) person -days for Ozone Dissolution System Install checkout of Manufacturer Proper Installation Five (5) person -days for functional and operation readiness testing for the Ozone Dissolution System 2. Phase 2: Inspection and Commissioning Five (5) person -days for installation assistance, inspectfinail onMOCP ntut ana d pre -commissioning of 03 Gen/PSU, Ozone Destruct, CW pump Ten (10) person -days for functional and operational Readiness adiTestess Testing for 03 Generation system equipment that is part of phase 2Perf One (1) trip of five (5) days on site for equipment performance testing 3. System Performance Demonstration Veolia shall perform the System Performance Demonstration testing in accordance with par. 3.03.E of section 44 44 56.11. 4. Operational Availability Demonstration (OAD): da continuous test shall be At the completion of the System Performance Testing a seven (7) Y run without significant interruption 5. Training equired Training as part of Phase 1 and Phase 2 as detailed In par. Veolia shall provide the r 3.04 of specification section 44 44 56.11 Note: Additional services if requested due to no fault of Veolia, are available at the rate of $1460 per day plus travel and living expenses. p. Work Not Provided Th e following items are not included in the proposed selling price and will be provided by others unless specifically called for in the body of this proposal: 20 of 23 Proposal 533310 Oshkosh FINAL_10-13-23.Docx A a. Equipment unloading, storage or erection. b. Interconnecting and intra-connecting electrical wiring except in skid mounted packaged equipment. p ged c. Interconnecting and intra-connecting oxygen, ozone or water piping and manual valves between the oxygen system components, ozone system components, equipment skids, contactors or ozone destruct system components. d. Wall sleeves and fittings. e. HVAC f. Control wiring or piping g. Insulation on ozone generators, cooling water piping, ozone destructors or other hot or cold surfaces (except ozone destruct vessels) h. Air, ozone, liquid oxygen, gaseous oxygen or water piping not on skids i. Anchor bolts j. Instruments and valves except as noted. k. Instrument air, instrument tubing or fittings (except on skids) I. Design, programming, testing or commissioning of any Control Systems other than those provided by Veolia. M. Power wiring and conduit, except on equipment skids n. Motor control center and local disconnects o. Field calibration of instruments not provided by Veolia P. Contact Chamber leakage testing q. Design of equipment not furnished by Veolia r. Cost for Power, Water or Liquid Oxygen (LOX) for commissioning and testing of equipment on job site. 11. WARRANTIES AND GUARANTIES The following are specific ozone system warranties and guarantees as required in specification par. 1.05 of 44 44 56.11: caon section 1. The equipment warranty for the complete system equipment is two (2) years from acce to of work or thirty (30) months from delivery of the equipment whichever occurs first p nce 2. Ozone Generator and Power Supply Unit power shall be as guaranteed in the Present Wo Evaluation Form presented with the bid documents. rth 3. Each ozone generator shall be capable of producing 600 Ibs/day of ozone at a concentratio 10% by weight with an open -loop cooling water temperature up to 86 " F. n of 4. Off -gas ozone concentration leaving the ozone destruct unit shall not exceed 0.10 ppm 5. Ten 00) year warranty on dielectrics and dielectric fuses. 6. Three (3) year warranty on power supply converters/inverters and HV Transform Proposal 533310_Oshkosh FINAL_10-13-23.Docx er. 21 of 23 OPTIONAL ITEMSISYSTEM ALTERNATES estimated 1. esign of As described in Item C above, Veolia has included ravni a that eitherst for Inc providing or Veolia adprovides the LOX and GOX field piping. It is not a normal as there is a lot of field responsibility that b�em but pipe design and field fit up should �pbe done s not our area of expertise. Sizing the p providing head loss calculations is no p by the Contractor as is the norm for all other'field piping. q deduct is provided to remove this service from our scope of supply. IV. CLARIFICATIONS AND EXCEPTIONS Clarifications: 1. The scope of supply in this proposal is based on the equipment detailed above and the highlighted P&ID drawings, highlighted Field Instrument list and highlighted named Valve list. 2. The supply of Liquid Oxygen for Commissioning and Testing shall be provided by the Owner. 3. Any field piping requiring insulation shall be provided and installed by the Contractor 4. Specification section 44 44 561 (ozone 5 fortheMOCP paragraph r02interface. Given the .0that use of Wonderware InTouch, version the ng WonderWare is no longer a brand name than isocurrrrentlygon themarket,InTouch version Veolia feels that any called for is a much older version t istake and as such, we we will be reference to WonderWare InTouch" was simply a m providing OIT programming using Schneider Electric Vijeo Designer, as it is referenced in specification 40 99 91 (Package Control System), under paragraph 2.03. Exce_ pt�ion_s_ 1. Veolia has taken no exceptions to the Specifications. 22 of 23 Proposal 533310_Oshkosh FINAL_10-13-23.Docx A SELLING PRICE: (To be advised) Selling Price: Item A — P Option 1: Deduct for removal of LOX/GOX piping Piping Design Total Selling Price (*) Note: Above prices are (exclusive of sales tax). to the invoice $ (See Bid Form) (*) $ ($ 52 400) (*) Should sales tax be required it will be added SHIPPING TERMS: DPD jobsite TERMS OF PAYMENT: (Recommended) 10% on Approval of Shop Drawings 80% upon shipment of equipment 10% on completion of Training and successful Performance Testing (not to exceed 180 days from delivery of the equipment) TERMS AND CONDITIONS: As per attached Terms and Conditions VALIDITY: Ninety (90) days from bid opening date BONDING: Not Included (Available at an additional cost —1 /° of selling g price) SERVICE: Field Service included in this Contract shall be provided for a period not to exceed * eight -hour man -days Provided in not more than * ♦ trips to check the completed installation by Purchaser, to place the Products in operation and to instruct Purchaser in their operation. Purchaser agrees to pay Veolia for any additional service days and/or trips in accordance with Veolia's standard service rates and conditions in effect at the time the service is performed. ♦ A minimum of one (1) full day of service will be charged to each trip. * See proposal details SCHEDULE: Approval drawings and data shall be submitted approximately (sere sche_d) weeks after agreement to all terms. Veolia estimates that shipment of the Products can be made in approximate) weeks after Veolia has received from Purchaser final approval of submittal drawings and data. (see schedule) PURCHASER'S ACCEPTANCE: Company Name By: Narneffitle Date: Ship To: SUEZ TREATMENT SOLUTIONS, INC. By: William Nezgod Senior Sales Manager — Engineered Ozone Plants Date: October 13, 2023 Proposal 533310—Oshkosh FINAL_10-13-23.Docx 23 of 23 ' 3icrr3a -}. 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U31N.N HSOMHSOjO All0 -- -- - OISIV31SASAUI M3N3O N011b-17d1SA up =1 rri W 1 3 1 i p �g 4N _ An a } CUR 4. z y' 1 f Ft .- t i f E (: `.( r : ( it pi it iii it !it : I (: - F I 1 fill 3 3 :( z- r, , _ c a t t _ -- 1 , .c < d ' [MIT t 38(llO311HOW W31SAS 108-LNOO 1OaL`'00 8 N'OLLtlLl3iYnN1SNi sgoae` Ooil i MA ""Elio = ei gg 5 O 5 O' _ �O1 8 It M 3 Avg mnuas t95HOOSU.1'HSOY.HSO a0 All0 srez w+todeu:�+.t+n 32iniO311HObd W31SXS 102j1N0O 3svH�ana H�va�ve vratsAs aHo�° wayr+o�arcatali+e+•�natstn LMId HO+ttlatlia a31`1M NSO4HS0 i0 /.110 sgOJe,f.'4 Ol SW31SASAUVI M3N d0 NOI1V77V1SNI Un? i9 TAB B - 2.2 PROCESS DESIGN CRITERIA PROJECT NAME: Oshkosh WTP Oshkosh, WI 2.2.1 - Ozone Generation Energy, Oxygen, N2 Consumption Ozone Generator Energy (Ea.) s) - 115 KVA (Active power at ;+N2) Oxygen Consumption (per 03 Gen) 50.3 SCFM @ 600 Ibs/day (0 89.8 SCFM @ 750 Ibs/day (02 + N2) Nitrogen Consumption Up to 2.3% by weight 2.2.2 - Gaseous Oxygen, Ozone Concentration Information Gaseous Oxygen Concentration Between 97.7 - 98.5% to the 03 Generator Ozone Concentration Design Concentration: 10% 03 Operating Range: 6 - 12% 03 2.2.3 - Liquid Oxygen Vaporization Rates LOX Vaporization Rates Design: 100.6 SCFM (6034 SCFH) Max.: 179.6 SCFM (10,776 SCFH) 2.2.4 - Heater Requirements for GOX Trim Heater Max Gas Flow 100.6 SCFM @ 1600 Ibs/day, 10% 03 (Max., Design pt). Max. Delta T - 80 deg F a Trim Heater Size 9.0 KW nominal power (smallest standard size) 2.2.5 - Ozone Diffusion, Headloss, Efficiency No. Of Diffusers per Diff. Cell 32 s Diffuser Flow range (min/max) 0.25 to 1.6 SCFM/Diffuser Headloss (min flow/max flow) - 14.0 to - 22.0 in. W.C. Mass Transfer Efficiency �900%%design diffuser flow rates SHT: CHCKED: PRELIMINARY TITLE: Heat Load of Ozone System Equipment 1 of 3 APPROVED: Veolto Treatment Solutions 1 EOLIA 600 WILLOW TREE RD. A DWG No. 14xxx-10-0600 REV: - er LE O NIA, NJ 07605 c o c U a1 @an 0 a Ew�+cmi aMy`` N 8 _ �a�.e EQoz° c c v O —m� aoizc© PROJECT NAME: Ozone Generator Vessel (Oxygen Inlet line) Oshkosh WTP Oshkosh, W1 The Gas Pressure relief valve sizing is based on the size and pressure with tin of the ozone generator alongi gas flow to be handled. Veolia has a Proprietary Calculation tool that determines the minimum orifice size for the required y necessary gas flow at the set pressure of the valve. This information is then used with the literature from the Valve Supplier (Kunkle) to determine the correct valve inlet/outlet connection sizes. SHT: 3 of 3 CHCKED: TITLE: UI ment PRELIMINARY Heat Load of Ozone S stem E REV: DWG No. V.OL Veolia Treatment Solutions A 14xxx-10-0600 APPROVED: t 600 WILLOW TREE RD. R LEONIA, NJ 07605 2.3.1 — Data Sheet OZONE GENERATING SYSTEM PROJECT NAME: Oshkosh Water Filtration Plant Number Units Oshkosh, W/ Three (3) Model Number SP-73 Ozone Generator Design Capacity 600 Ibs/da ° Y @ 10 /° 03 Up to 750 Ibs/day @ 7% 03 Ozone Concentration Operating ~ 6.0 to 12.0% by weight Range g Feed Gas Source Gaseous Oxygen (GOX) Feed Gas Inlet Temperature ~ 86 OF Feed Gas Dewpoint -76 OF (-60 °C) or lower Feed Gas Flow Rate (design) 50.3 scfm @ 600 Ibs/day @ 10% 03 89.8 scfm @ 750 Ibs/day @ 7% 03 Feed Gas Quality Oxygen ~ 98% Nitrogen ~ 2% Materials of Construction Vessel 316L S.S. 02/03 Piping 316L S.S. Type of Cooling H2O Piping 304L S.S. all Closed Loop Heat Exchanger Design Pressure Rating Oxygen Side 50 psig Water Side 50 psig Pressure (g Operating Presss roaa a ) ~ 21 psig a "`z Connection Sizes: Oxygen In ° 2" RF 316L S.S. (Gen. Skid) Ozone Out 2" RF 316L S.S. N Water In/Out 2-1/2or 3 " " RF 304E S.S. �� ¢© POWER SUPPLY UNIT (PSU) v ° Power Su pply Units No. of power supply pp y units installed Three (3) Model Number Note: PSU is located on generator skid Type of PSU IPS-16-0200-WC-12 Medium Frequency DATE: 09/13/01 TITLE: Ozone Generator S ecifications SHT: APPROVED: � Of 3 VEOLIAVeols Weter Technologies g Solutions DWG No, WILLOW TREE ROAD A 14REV: LE XXX-02- LEONIA, NJ 07605 01 00 - 2.3.1 — Data Sheet OZONE GENERATING SYSTEM PROJECT NAME: Incoming Power Power Factor Converter/Inverter Type Ozone Generator Rated Capacity at full power Ozone Generator Voltage Ozone Generator Frequency Enclosure Type of cooling Cooling water flow rate to PSU Cooling water temperature increase Cooling water inlet/outlet Cooling Water Headloss at max Flowrate rN aximum Heat Rejection into Room oise level from PSU at 3 ft. Cooling water source Ambient temperature Oshkosh Water Filtration Plant Oshkosh, WI 480V/3 Ph/60 Hz > 0.98 cos phi or higher Insulated Gate Bipolar Transistor (IGBT) 600 Ibs/day @ 10% 03 Up to 750 Ibs/day @ 7% 03 < 4,000 V RMS Up to 1450 Hz NEMA 12 TABLE 1 INFORMATION REQUEST 2.3.1.A Total Connected Load 2.3.1.B Power Requirements at 03 Gen rated capacity, max. CW temp Internal Heat Exchanger + recirculating blower + water chiller 8 gpm (flow included above) —8OF — N 1 in. RF s 5 psi < 5,000 BTU/hr < 85 dBA Same as Ozone Generator ---- 110 OF T7.8 DC max. max. Active Power ~ 120 KVA 4.45 Kwh/lb 03 @ 600 lbs/day, 10% DATE: 09/13/01 TITLE: Ozone Generator S ecifications DWG No. VEOj Veola Water Technologies & /� 14xxx-02-0100 APPROVED: LI Solutions / 600 WILLOW TREE ROAD LEONIA, NJ 07606 SHT: 2 of 3 2.3.1 — Data Sheet OZONE GENERATING SYSTEM PROJECT NAME: Oshkosh Water Filtration Plant Oshkosh, Wl 2.3.1.0 Max. CW flow rate and temp rise through 03 Gen/PSU Max. flow rate: 88 gpm Includes PSU Max. temp rise: 8.0 °F (600 ppd 10%) Closed -loop CW temperature to Ozone Generator and PSU Minimum CW pressure to skid 2.3.1.D Supplemental Cooling requirements for PSU 2.3.1.E Total Weight 2.3.1.F Performance Curves 2.3.1.G 89 OF based on a max. open -loop CW temperature of 86 OF 20 psi None (included in the above flow rate) Shipping: Operating: vessel — 14,600 Ibs vessel Flooded: — 15,800 Ibs vessel — 17,200 Ibs See attached curves @ 10 and 7% at Different CW temperatures Complete Inverter rating 200 KW Active power at generator (Special features of Converter/Inverter is attached) 2.3.1.H All necessary info on HV See attached drawing transformer c 2.3.1.1 List of Spare Parts y U 1. Assemblies: 5 percent of one generator load, beyond those broken during initial shipment or installation. v 2. Dielectric Fuses (If Used): 10 a ti a 3. percent of one generator load. Head Gaskets: Two per 4. generator. Sight Glass with Gaskets: One � 5. complete replacement set for one ener. g ator. Fuses: One complete replacement set for a.o.y 6. 7. one generator. Complete circuit board replacement set for one PSU. Two sets of air filters for v = o�mc 8. PSU (not required). Special Tools: One complete z Q 9. set of special tools required to dismantle equipment. The Seller shall supply its own ozone wet test kit ° ili � o .� and dew point cups during startup and performance testing. These instruments shall become the property of the O field testin and startu .� r a 2 +° 3 U caner following DATE: 09/13/01 APPROVED TITLE: IfOzone Generator S VEOr So lu tl ons ter Technolog(es & i 600 WILLOW TREE ROAD LEONIA, NJ 07605 ecifications A I 14xxx-02-0100 SHT: 3 of 3 N moo©©©©e •-•ter-aaav�w�wvlrro= !-' gYOW WZN�VZ-��y6 z o zzuu3��aQc�c=.>¢a W Z W - I r z � I] z F— —J Lj Z W f— l-0 =D C7 W N q O Y I 7xi r- ur+ 9:E a n Imn C C r" I to d Ci rt qzj- w koo. M � O (qi/4AA I) uoRdLunsuo:) jamoe, A m a i U) n I x M Ci Q J W N � X U a LI N � N� W n' o a N E m lU c z �� m 0 'u= 00 0 I 0 0 00 � `° `*• m m �o N cn M m (gi/4M)l) uoiidwnsuo:) aamOd 0 0 0 Q (j) V E O ll A Product Data Sheet I -Stack 2W th ReaIS nee"" Technologyower Converter — IM13001OWN1 This I -Stack is a CE-certified fullyintegrated volacv - source power converter featuring a rectifier and an H-bridge inverter with a technology D intelligent in between. It is based PWM processor board. Proprietary control provided by factor near RealSineTM technology maintains the power unity while easily meeting IEEE-519 harmonic distortion requirements. The t-Stack features integrated voltageleafiteringcurrent to monitoring, auxiliary controls, and ripp ensure that it can be installed in most electrical environments. A single I -Stack can handle up to 200kW but when grouped using a proprietary paralleling technique, an I - Stack -based Power Supply Unit (PSU) with multiple power stages can control multiple megawatts of power. As each power stage is independent, this increases the total system availability and ease of maintenance while receiving its setpoint from the OGU controls. It can be operated locally using the web serverh a PC a matching smartphone as well. For Ozone applications, a a of the transformer is used to increase the output9 I -Stack to over 6kV. Features ■ Very low harmonic generation on the line. ■ Power factor close to unity over the operating range. Modular PSU design increases system availability. ■ Integrated front -mounted control fuses for accessibility. ated contactors to operate auxiliary loads. ■ Integr ■ Digital control by a processor for fast reaction to process changes. d ■ High DC bus capacity to handle low power factor loa s. • More than 200 different warnings and alarms to accelerate troubleshooting. ■ Pre -charge circuit integrated. ■ Derive the main contactor coil power from line voltage reducing the load on the 24VDC supply. 25/11 /2022 IMB0010147_PDS_EN V1 Product Specifications / Rating plate VEOLIA Nominal Output Power: Voltage (RMS): Max. Current (RMS): Frequency: Protective class and overvoitage category: Residual current: Auxiliary Power: Main cont'actor o l; Power Connections: Enclosure type: Altitude for insulation coordination Storage Temperature: 0°C to 50°C (32 to 122°F) Ambient Temperature: 50C to 45°C (A to 113°F) Relative humidity <65% on an annual average, <85% on 60 days of the year. The Dew point must be above the cooling water temperature. No salt or conductive dust is allowed (3K3). Pollution degree 2 as per EN62477-1:2012 5 to 30°C (41 to 860F), a corrosion inhibitor may be required in certain environments. Keep above the surrounding air dew point to avoid condensation. 0.1 to 1.8 m3/h (0.5 to 8gpm) 380kPa (55 psi) 586kPa (85 psi) 3/< FNPT located on the left side when looking at the control fuses while the I -Stack is sitting flat on a table Locate in a vibration -free environment Air Quality: Cooling Water (CW) Temperature: Cooling Wate- F Nominal CW Pressure: Max. CW pressure: CW Connections: Vibration / Sh co k Veolia WTS, 5490 Thimens #100, Montreal, QC, Canada, H4R 2K9 Tel: 514-337-7979 200kW @ 480VAc Vin: 208 to 480VAc (t 5%), 3PH TN-C Vo Efficiency: 750VAco 1 PH lin: 250A @ 480 VAC, CWT 30°C Fin: 50 / 60Hz (t 2%) lout: 440A (650A pk) Fout: 0.1 to 1.5kHz ------------ Class 1 as per EN62477-1:2012 Overvoltage category II This product can cause a DC current in the PE conductor. Where an RCD protection is used, only an RCD type B is allowed on the supply side of this product. 24Vdc, 5A+ external loads if applicable Line voltage L1-L2 through internal 8A control fuses and relay 25mm (1") Bus -bar C/I/V 8.5mm (0.33") connection holes Open chassis, IP00 Up to 3000m IMB0010147_PDS_EN V1 25/11/2022 ypical Connection Diagram cabinet Ethernet I — ' - ' - — i — — Bridge Control sup rk Ip Board 4 �, temperature, Air flow, 1 connection board Transformer to OGU protections I controls j - --- - j t - y - - W2 - FU11 C�1 LC11 C� T ,�y T t f� tozone i O I Gl 1 I t PWM board -Stack generator I -•------------------ 24V Supply i • HV 1 000 °00 0000$0 000O000000� Three- Temperatum feed j O00,O°000001 phase contfoi valve back 0oo00,D00,oD00,000oD00po00, supply O00g°o-g0-000 I I 1 00000 1 Tuning I j inductor j Powerstage _.—.-----.—.—.—.—.—•--' — Note: Suitable enclosure, main contactor, line fuses, cooling media, and load must be added to the I -Stack for proper operation. See the installation manual for moredetails. Dimensions MODEL IMB0010147-VI water- cooled �/57 H HEIGHT WEIGHT LENGTH 81.6 Ibs/37 kg 22.22 in/56.4 cm 2cm 11.17 in/28.4 cm IM60010147_PDS_EN V1 25/11/2022 ipi w xruei2-f4.ume �`a c; a r ( e 7�rwa Elf a axr, e, are &Oft scv3�°�' �, .a �hra�-w. ryy.- w��r�� mf.l a � t¢3 E�6 #pp e't rr a+s0.� PoC.; fiJ roA dab # aaa3 tb «. n: ruw re.CY,� f? - r L UI? yr 9E.. bk,1- `� R �d ►�4w mo Mi �dq�u� z Bo�.a� MODEL DESCRIPTION DIMENSIONS IMD0010746 DVI connector terminating resistors 55mm L x 40mm W x 15mm H MODEL IMD0010756 MODEL IMD0010759 DESCRIPTION Digital dual -link cable, DVI interface DESCRIPTION Digital dual -link cable, DVI interface © Copyright Veolia WfS 2022 All rights reserved. This document may not be reproduced or copied, in whole or in part, in any form or by any means, graphic, electronic or mechanical including photocopying, recording, or storage in a retrieval system. lMB0010148_l`DS EN VIA= DIMENSIONS 1830mm L DIMENSIONS 914mm L Veolia WiS reserves the right to change the characteristics of its products and services at any time in order to incorporate the latest technological developments. The information contained in this document Is therefore subject to change without notice and cannot be construed as any form of contractual obligation. IMB0010147_PDS_EN V1 25/11 /2022 �ProductDataSheet High Voltage Transformer Series IMD0010713 High voltage transformer for one phase Ozone Generator 1450Hz, 280kVA, dual isolated primary coils. Features/ rse,-,1 • Air core connection tap ■ Adjustable taps ■ High frequency transformer 0Dry type transformer • Temperature protected :s: ,tinn rrouUUL JN-„..,„�.. Cooling Type Forced air (3m/s) Secondary Power (Sp): 280kVA Dual Primary Voltage (U1): 740V / 1phase Secondary No-load Voltage (U2o): 2792V / 1 phase Operating Frequency (f)' 1450Hz x ( 0A 2) 19 0A Primary Current (at full load) (IP): Secondary Current (at full load) (IS): IOOA Temperature Switch (24VDC, 0.5A, NC) (SW): Yes 115°C Temperature rise (Max.) Jr): Wiring and connection material Copper C293 Weight Kg Ambient Temperature °C 50 Isolation Class H Standara 0 IEC:60076-11 Dimensions All dimensions are in mm. 2 iERNINAIS C SES SEPANAtELY�SUPPLIEDWiTN THESEtAffACNENENtS © Copyright ImalogTm Inc. 2016 ION DUPE PANEL All rights reserved. This document may not be reproduced or copied, in whole or in part, in any form or by any means, graphic, electronic or Imalog, Inc. reserves the right to change the characteristics of its products mechanical including photocopying, recording or storage in a retrieval y time in order to Incorporate the latest system. no services at an technological developments. The information contained in this document File: IMD0010713_EN_PDS_RevO.docx is therefore subject to change without notice and cannot be construed as any form of contractual obligation. PROJECT NAME: DATA SHEET — LIQUID OXYGEN SYSTEM Oshkosh Water Filtration Plant LIQUID OXYGEN STORATE TANKS Oshkosh, W/ T4007-1, T4007-2 Number of LOX Storage Tanks Two (2) Storage Tank Volume 9,000 gallons Storage Tank Configuration Vertical Maximum Working Pressure 250 psig Dimensions (Approx) H 348" Weight (Approx) D 114" Empty 32,300lbs Connection Sizes Full LOX 120,300 Ibs Fill Valve 1-1/2" Bronze Liquid Withdrawl OXYGEN VAPORIZERS 1-1/2" Bronze Number of Vaporizers M4017-1, M4017-2, M4017-3 Three (3) Manufacturer Thermax Model Number Type of Vaporizer SG140HF Ambient Vaporizer Capacity 120 SCFM (7200 SCFH) ma'a e . (1.20 x 1200 Ibs/day) ''° '= Design gn Pressure @ 10D/0 a.o , N ,y Q 450 psig -�rz Normal Operating Pressure C C N N o Dimensions 75 psig z�Qo L 48' W 48„ H 213" Weight 760 Ibs CHCKED: PRELIMINARY TITLE: APPROVED: Li "' OX en S stem SHT: 1 `� gsly Y LIA of 3 "I WILLOWTREEROAD /es DWG No. LEONIA, NJ 07605 A 14XXX-77-0100 REV: - PROJECT NAME: TRIM HEATER Manufacturer Model No. Quantity Flow Capacity Heater Size Input Power Dimensions OXYGEN FILTER Manufacturer Model Number Quantity Design Flow Rate Dimensions Connection Sizes Weight Oshkosh Water Filtration Plant Oshkosh, Wl Thermax TBT9 Two (2) 100 SCFM (design @ 100/0) r480V, KW (smallest heater size) 3ph, 60 hz, 11 Amps x 36' x 62" HT PRESSURE REGULATING VALVE Manufacturer Model Number Quantity Connection Size End Connection M4039-1, M4039-2 Graver Consler YCP110-010FL/0206 Two (2) F100 SCFM 4-1 /2" OD x 25" H V' R F 35 Ibs PCV-4043-1, PCV-4043_2 Caschco SLR-2 Rev. A Two (2) r�4 in 150 lb FLG 2of3 TITLE: en S stem CHOKED: 1 I uld OX PRELIMINARY L.. DWG No. O� oO VEOLIA Water Technologies A 4xxx-77 APPROVED: - I 600 WILLOW TREE ROAD xs•� LE NIA, NJ 07605 PROJECT NAME: Material of Construction Design Flow Rate Inlet Pressure Outlet Pressure PRELIMINARY Oshkosh Water Fi/tration Plant Oshkosh, W/ Body Stainless Steel Dome Stainless Steel 8.0 to 170 SCFM 50 — 100 psig 22.0 psig APPROVED: Li Uld OX en S Stem VEOLIA Tech, VEOLI, 600 WILLOWeTREE ROAD Jes DWG No. LEONIA, NJ 07605 A 14XXX-77_01 00 3 of 3 L I S I --- ----------------- I I I I i I e I 1 1 I I I 1 mg as I `Cfl I ____________________-- - „-$ I I I Y I I111 I + I I 11 Zm Ii QyOa ' i a I II �------------- i I S I I I1 a I i ( 1 I I I � � I � }I ( / `- .i 1 ---:----, ---------a � I ) I I { \ ! \ | \ § _ aof �q o�� m� � ��� Y WNW � o W m \ > \ ■ 3: � k 6inp Z ^aa t00-9t0-Zl0-LOSO\SS6SJ4 P°°D 6 B f t 9ISd 099 9ISd 009 S S 1 d'd N0139VMS \ \ L-0OO� '1'd'W 9t 4 l t 9ISd S'S NOl39VM5 099 9Sd 009 SSVBB 1'd'd NOl39VMs 6 Z 9ISd 099 9ISd 009 3gNY1i31� °v° a �_9L-9l-L�BI 9{ 6 Z 9ISd 098 9ISd 00g 39NV1d 'ON aor :na M'd'a OOf .9t/6 Z 9ISd 099 9ISd 009 ON3 BftlS'WOnr//�•0� 1NIOP dVl'S'S ,B/L 9ISd 964 M'd'd 00£ON ,Z l 9ISd OS; •0'0 2i301OS 8 l-1 OISd S64 Np JMc W W } � ' m .91/6 Z AOOf 9ISd f0£ 95d 9LZ ON3 BfllS'WOIV 0-Li 1N dVlS'S i609t 9l L t 9ISd 099 9Sd 9ISd OS4 39MNy'ti S•ja OOf ,BZ£tZ 9ISd S64 9ISd 094 39NV1i 0 S'd'j 00£ OISd L6Z OISd OLZ 39Nyld o M o` lR 0 009 9l L l 9ISd 099 9fSd 009 S'd'I O139 13NO0S 9t 9 9ISd 099 9ISd 009 3lVW3d Td'N'd 'S'd'I ,B £ Z Z t 9ISd L6Z Sd OLZ 39NV1i M d a 09t 9ISd f0£ 9ISd SLZ 39 Md'd 091 Z l 0 p O \ N tW-O� Q Ol3A llO8 380SS32id 3NOSS3Md 1S31 N91S30 3dU NOLL93NN09 9ISd £0£ 9ISd SLZ 39NV� S'd'21 091 9t 9 9 Sd 099 9 S NVId 0 S'd'd OSl 38nS 0!S ld O \ ¢ \ C 1. U Q Q f` I.L. SNOIldO 318b11b'ny- 31�03HOS wV 3Nf)SS3Nd H N91330 3d11 NOLL03NNOD N01103NN001VN1WON �; E O (n „ ,/C sn [l47 9NV8 4; 9NV8 04 BfllS 1M01` 9MN [967 ouv 44 9NV8 0; . L — 2 v 9ISd B£9 9ISd OBS 3SOOIWn� 3N1S3121d 3N(1SS3Nd S S 04 d SZ 0 8 £ £ 9ISd B£9 9ISd OB9 SS b U1U Z % %pl 96 ONVB 14 9NV8 04 E.�' L. ,q, N91S30 3dti N01t03NN00 £ 9ISd B£9 OISd 069 .y 3NfISS32id 3N(1SS3Nd WfilV • l - 021ds8 EE C ,v^ o 01 (n V I m 0•- N > SNOIldO 3l8bllt/AtJ- 31f1a3HOS N01103NNOON$Qyya f13 E'er N f/1S E 0 uiF wW O O W J \ U � W J W = v U) ZZWLjm}W FNO-p�V- N DpjXZ}2OWZ �NU�JQN(n LLj 3�W2Z_�V)¢ -QZ)-�(W,l LLI F 'O¢w¢z ZZ�c U Q U b O M N L Q u Q O nxoee \ U' u � y Q t m W .JI ~a J�4 v fa W � tt `� Ld O J L V N u J W V to V91N Wd1�03 d VdOS01�130378.3W aPlVld N/ONb �N3JOAa� �yOH Ol3LNOIN� SUO d N�0 VH `JNINNWAA I 9 THER-M48ILOCK"' VAPORIZERS 41�. Cooler By Design.. Thermablocklm Electric Vaporizers cryogenic To act size and provide reliable and e a e° ThetThermablo�k o has af a dcomvariety o cryog liquids and liquefied g in bring in a single simple installation. Connect the inlet grate. These electric units vaporize power line and the unit is ready to op cycling the liquid and provide superheat, warming the gas for downstream processes. The outlet temperature is loop using an maintained by y the heaters on and off via a feedback loop using temperature controller and temperature probe. CONSTRUCTION: Stainless steel heat transfer tubes aed between extruded aluminum nd weather -resistant, e electric cartridge heaters are clamp enclosed blocks. Controls are sepe oof tecabinetsinto g A temh and 1peratuow lre probes used for precise temp In NEMA 4 rate temperature control. Optional Features temperature Low Temperature Cut Off (LTCO) Kit featuring a temp as or sensor and solenoid valve to prevent the flow of cold g of the vaporizer, 500 PSIG design pressure liquid downstream PB solenoid valve trey°untrol re b ulderspressure building circuits on combo units and p Produc t Datasheet IJ Standard Features • Replaceable stainless steel cartridge heaters • NEMA 4 Electrical Cabinet • Adjustable outlet temperature from 40°F to 120°F • Fully automatic operation • Compact design • High temperature switch for safety • Thermablock" all comes fully factory wired, tested and ready to . quick delivery of standard units • Built in accordance with ASME B31.3 Process Piping Code wetted arts Desiggnn pressure of 1,000 PSIG (TBTL/316 series Stainless ITBV) and 500 PSIG (TBC,TBP) • The electrical cabinet is UL/cUl marked • Pallet base • Pressure switch to control ressure on combo and pressure bupd modelbuilding circuits �-. Cooler By Design.. VAPORIZERS THERMAE3LCICK,, ELECTRIC retUCESS VAPORIZERS Model Nominal 208 Voltage Power (kW) Item 480 N2/02 capacity p Y TBV9 9 Number Number Item Amps Number CO2 Capacity (SCFH, liquid) (Ib/hr, liquid) Uncrated ) TBV15 2156 Amps 25 21553455 q HxWxL (in.) TBV30 15 30 21562051 11 42 21547647 19 2600 180 TBV4040 21562052 83 21553456 4400 300 62 x 36 x 36 TBV60 60 NA NA 21553457 49 8850 600 62 x 36 x 36 NA NA 21553458 73 11,800 800 62 x 36 x 36 17,750 1200 62 x 36 x 36 62x36x36 Nominal power, Model Process Nominal Power, Pressure COMBO VAPORIZERS Voltage (kW) Build (kW) 208 480 N2/02 Process N2/02 PB TBC20 T8C40 15 30 Item Number Amps Item Number Amps p 5 21563474 56 21553464 Capacity (SCFH, li uid Capacity q ) (SCFH, liquid) CO2 process CO2 PB Capacity (lb/hr, Capacity (Ib/hr, TBC60 50 to NA 25 NA 21553465 4400 1450 liquid)Uncrated liquid) HxWxL (in.) 49 NA NA 21SS3466 73 4 7r0 2950 14, 750 300 100 600 70 x 36 x 36 2950 200 1000 70 x 36 x 36 TRIM HEATERS 200 70x36x36 Model Nominal Power Voltage (kW) 208 TBT9 Item Number 480 - N2102 Capacity Uncrated TBT15 g 2156206/ s Item Number 25 (SCFH, gas) Am s H x W x L (in.) TBT30 15 30 21562061 21562062 21553459 42 21553460 11 12,000 19 62 x 36 x 36 TBT40 TBT60 40 NA 83 21553461 20,000 37 62 x 36 x 36 60 NA NA 21SS3462 40,000 49 62 x 36 x 36 NA 21553463 53,450 73 62 x 36 x 36 80,300 62 x 36 x 42 Model Nominal Power PRESSURE BUILDERS Voltage (kW) 208 TBp9 9 Item Number 21702513* Am s 480 p Item Number N2/02 Capacity (SCFH, liquid ) CO2 Capacity Uncrated TBP18 18 25 21702514* Amps (lb/hr, liquid) HxWxL (in.) TBP30 30 21702516* 21702519* 50 21702517* 11 2600 22 180 73 x 52 25 83 21702520* *Standalone models 5200 37 8850 x 360 73 x 52 x 25 600 73 x S2 X 25 Key features • Replaceable heater cartridges • External temperature controller Chart Inc. U.S.: 800-400-4683 Worldwide: 952-243-8800 Cooler B D i � r � esign. e _ - --i I or• Mode! © 2021 Chart Inc. P/N 21568190 www.chartindustries.com o z I �o @ A C, Q RZ2 Z o Q <zOo z I MINIIIIIIIIIIN 0 z LO u V) os 04 0 > z z We) 3: z Lu Z5 co 'Eu lao GG L) c) IN z w Z00-- z gzw 03: @ w -, > < � (D oa-0 =) 3 0 :-z J� .: U!�� Z- 0 < ,- 86 -c',,0 7 P to R 2 - LU , 0 w 09 w 2 Z.) -zi w < o u 06�:>:oZ<%s dlqwwo (D�E3: 62W LU < Wb z ZZ@(L�d 0 0 W<L ca a ISO Registered Company MODEL SL PRESSURE REDUCII` REGULATOR WITH NON -RELIEVING OVERVIEW LOAD Model SLR-2 is high performance, pressure loaded diaphragm -type Design includes flow -to -open pressure reducing regulator. an internal pressure balancing piston-cylin that provides high flow capacity and high pressure drop capability. Performance meets or exceeds that of competitA pressure loaded or pilot -operated designs. A non -relieving Pressure regulator "loader" is bracket mounted to the top of the dome. The set point of the loader controls the upstream supply pressure into the dome to maintain the desired downstream pressure of the SLR-2. Pressure in the dome w constantly bleed out through a filter and check valve which is Piped back into the outlet of the body of the pressure reducin regulator. FEATURES Versatile: Five basic materials and multiple trim material combinations to select from. Multiple methods of Tight Shutoff: pressure loading. Multiple Composition materials provide Class IV and VI inboard leakage rates. Designed as a soft -seated valve. Capacity: Highest in the industry. Allows smaller body sizes than competitors in majority of applications. Droop: Highly accurate outlet pressure control, due to absence of range spring in desig n, Provides almost zero "droop effect'. Trim Design: FTO and pressure balanging allows for higher miet pressure. Results in unmatched sensitive and staff, Internals are cane -contained within easily removable Cuick chime tr__im Rangeability: Basic valve gives outstanding rangeability due to close tolerances, balanced trim, and broad range of elastomertc and metallic diaphragms and soft seats. Can be as high as 2000:1. Heavy -Duty Guiding: Both top and bottom guided to maintain stability and increased diaphragm life. Failure Position: Fails closed on loss of loading pressure. APPLICATIONS Designed as a gaseous service regulator. Excellent for atmospheric industrial gases — GN2, GOX, Ar, He, H2, CO2 — as well as natural gas. Can be used as a utilities air regulator. Also for use in corrosive and non -corrosive chemical gas services are Possible with broad materials range. TECHNICAL BULLETIN SLR-2-TB nq_?n STANDARD I GENERAL SPECIFICATIONS Body / Cover Dome Materials Pressure Drop Limits Z SST/DI 5-1500 psid (.34 —103.4 Bard) DI/DI BRZ/BR SST/CS d base trim material, dia- CS/DI BRZ/DI CS/CS SST/SST DI = Ductile Iron CS = Carbon Steel BRZ = Bronze SST = Stainless Steel Body Sizes 1,� 1-1/4", 1-1/2", 2", 2-1/2", 3' 4 1 /2", 3/4 , 65, 80, 100) (DN15, 20, 25, 32 40 50 End Connections Standard: Female NPT. ASM_a nged: 125#, 150#, 250#, 300#, 600#; PN25, PN40; DIN F_ I_ a_ raged_: PN16, (Integral Flanged Body unless listed under Opt.-30) Opt-31: British Standard Pipe Threads. ads. ion. Opt-34: 14 Face to Face Flange Max. Useable Cv See TABLE 7 for Wide Open Cv Limits. dy Size Comp. (DN) Cv" (50) M 54/2, (65) 81„ (80) 1084° (100) 198 METRIC CONVERSION FACTOR:F_ Cv / 1.16 = kv Max Operating Pressure 3600 psig (248 Barg). See Tables DAG-1 A thru-1 H for design P vs. T limits Function of service flue , phragm and dynamic seal design. See TABLES -2, Temperature Range -50° to +400°F (-46° to +204° C) Limited by body/cover dome/diaphragm material com- binations, and by elastomeric seat, static seal, dynamic seal —materials. SeeTABLE 1 Athrough 1 F andTABLE5. Alternate "CS" Mat'I - Steel - A4TMC) 352 Gr. LCC - Minl'mum temperature -50 IF (- 6Inboard Leakage Rate See TABLE 10 -- Lower Plilston Spring No lower piston spring; P2 = PLoad• Lower piston spring required; P2 < PLoad- See TABLE-9 for available spring ranges. applications: NOTE: Use alower pis'pmay reach 0 ps'►gfollowing app 1. When decaying nle optional Constructions O_ 30: Weld -on Flanort ges Qp 85. Extra Set PreDiaph ssure OQt-31: BSP End Conns. — s Oft-34: Special 14" F to F Tap PE551 Oxygen Cleaned OQpt-56.. Special Clean Loader Specifications Globe Design. 1 /4" Size, NPT connections. Available in Aluminum, Brass or SST materials of construction with NON -Relieving feature. Range springs from 0.5 to 1250 psig. (See Position 13 on the coder.) Outlet Pressure Range Loader Max. Pressure Outlet , inlet 0.5 - 1250 psig ( 0.03 - 86.1 Barg). on selection of Loader Material psig Barg psig Barg Multiple springs - ranges dependent 13 on the coder. 500 34.5 400 27.5 the unloader. See Position ALUM 248 750 51.7 diaphragm material. See TABLE 6. BR 3600 3600 248 750 51.7 Function of SST 248 1250 86.1 SST w/ SLR-2 -Opt-81 3600 -------------- 1-1 FK = Fluorosilicone FKM = Fluorocarbon EPR = Ethylene Propyl( BC = Neoprene ABBREVIATIONS NBR = Buna-N RTFE = Brz-fill TFE GF-TFE = Glass -fill TFE PA = PolyAll PTFE = Foiyieuaouv,��•,•, - V-TFE = Virgin TFE CTFE = Chlorotrifluoroethylene MATERIAL SPECIFICATIONS Body �► — ASTM A395 Diaphragm CS — ASTM A216, Grade WCB. Alternate ASTM A352 Grade LCC BRZ — ASTM B62, Alloy 83600, SST — ASTM A351, Grade CF3M. See TABLES I through IF for material specs. Cover Dome �► — ASTM A395 CS — ASTM A216, Grade WCB. Alternate ASTM A352 Grade LCC BIZ — ASTM B62, Alloy 83600, SST— ASTM A351, Grade CF3M Metallic Trim I'►u Ca e: 17-4PH SST, 316E SST, Nickel -Copper Alloy (Monett), PART TRIM DESIGNATION Plug Guide P 17-4 PH SST M Monet t S 316L SST T 17-4 PH SST 3earing 17-4 PH SST Monel t 316L SST 17-4 PH SST Cage Body 316L SST Monel t 316L SST Monelt ushing 17-4PH SST Monel t Monelt Monelt I FLOW DIRECTION Elast---i — BC, EPR, FKM, FK, NBR, FKM+TFE. Se�=�= POIyAE::II, V-TFE, GF-,TFE, BC, NBR E::::Static Seals (See Fig.1) NBR, FKM, FK, EPR - 0-ring SSTITFE (1/2"-2") (DN15-50) sizes, V-TFE (2-1/2"-4") (DN65-100) sizes. Dynamic Seals (See Fig. 1) T—YPee__QR - NBR, FKM, FK, EPR - T e UC p o-ring seal. iyP — V-TFE u-cu seal w/316L SSTenegizer — V-TFE u-cup seal w/ Elgiloy energizer Tvo—� — TFE cap seal with o-ring energizer (o-ring material same as static seal) and GF-TFE wiper backup seal. Painting Standard: All non corrosion resistant portions to be painted with corrosion resistant epoxy paint per Cashco Spec #S-1606. ' See Product Coder for acceptable combinations. t MoneITM and Inconel® are registered trade names: MoneITM is a mark owned by International Nickel Co. Inconel° is a mark owned by International Nickel Co. own with Lower Piston Spring. Body Material Specifications es A182 Gr. F 316L Cast Stainless St eel A351 Gr.CF3M or Stainless Steel Weldment A315 Gr. CF3M w/ forged flang I S ecifications Topworks Mater►a p Cast Stainless Steel A351 Gr.CF3M ESIGN PRESSURE vs. TEMPERATURE s ENDe NOTE CONNECTION RATINGS D (Per ASME B16.5 and - TABLE 1 E DESIGN INLETPRESSURE in PSIG (BARG) END CONNECTIONS CONSTRUCTION STD DIAPHRAGM DESIGN TEMP. RANGE: Deg F (D _50 to +100 (46 to +38) 20 (-2 .20 to +300 (.29 to +149) -20 to +400 (-29 to +204) CONSTRUCTION DESIGN TEMP. RANGE: Deg F (D _50 to +100 ((-46 -20 to +200 ('2 -20 to +300 ((-29 -20 to +400 (-29 to +204) NPT, BSP 1440 (99.3) 1240 (86.1) 1120 (77.1) 1025 (70.9) ALL Opt-81 (Full Support Diaph.) 150# 300# NPT, BSP 600# 1440 (49 6) 3600 (248.2) (99•3) ( 19 0) 3095 1240 235 (16.5) 43 0 ( ) (21620 5.1) (86.1) 2795 ( 14 8) (38 6) (192.9) 77.1 (77.1) 2570 1025 13 6) (35 5) (177.4) (70.9) TABLE IF SURE DESIGN IOPU (BARG) END CONNECTIONS Opt-81 (Full Support Diaph) STD ALL DIAPHRAGM NPT, BSP, NPT, BSP, 150# 300# 600# 600# 1125 625 275 43 0) 625 ( ) ( (77.5) (43.0) 235 1125 620 620 0(77.5) (16.5) (42.3)1120 (42.3) 560 215 560 (14.8) (38.6) (77.0) (38.6) 1025 515 195 (35.5) 515 (70.9) I'A5.5) (13.6) Directive e further Berated by limitations through the are those which ch areessure tlowest for the two materials. NOTE 1: These pressure ratings may b lied would have a preliminary 400 psig. Must derate both the inlet and d be standard diaphragm construction, at 200 deg F maximum temp to works material Whenever body and topwored SST body, the P vs. T ratings that shou�essureprating is only Exam le: 300 lb. RF flanged works p inlet and outlet to 620 psig, but if fitted with a ductile iron top outlet to 400 psig• (No te: Topworks pressure rating, same as NPT design outlet pressure rating for the selected and diaphragm type. The ratings are the same d above, if substitute lonr topwork products. material. 300# Flanges are Berated due to the bolting SLR-2-TB a DIMEN. END CONN. r dI NEM SIGN and WEIGHTS ENGLISH UNITS (in) (Ibs) BODY BODY SIZE MAT'L 1/2", 3/4 1-1/4" & & 1,, 1-1/2" 2" 2-1/2" 3" DI, BRZ 6.00 9.88 9. CS, SST 8.25 _ _ 9.88 9.75 DI DI _ 10.88 11.75 1, BRZ t* 9.63 - 11.50 12.50 1, 11.50,j 11.50 BRZ " 9.63 10.88 11.75 1; 11.50 J 11.50 CS, SST 10.75 11.50 12.15 14 12.38 -,/ 10.00 CS, SST 14.00 10.88 11.75 13 14.00 J 14.00 CS, SST 10.75 _ _ 12.38 -I( 10.50 11.50 CS, SST 14.00 12.50 14. 14.00 � 14.00 CS, SST 10.75 _ 12.38 / 11.25 12.25 'S, SST 14.00 13.25 15.; 14.00 V 14.00 ALL ALL 9.50 10.00 10.25 11.75 13.25 13.2 ALL 2.84 4.50 3.69 4.00 5.25 5.75 7.0( ALL 4.75 5.13 6.25 6.63 6.63 ALL 2.25 3.50 3.75 3.75 4.25 4.25 ALL 6.88 4,75 7.38 8.13 9.13 9.63 9.63 ALL 6.44 4.75 6.00 4.75 4.75 4.75 6.25 6.25 8.50 8.50 8.50 ALL 26 35 51 1LL 31 45 ad - . _ MFT01f% i sh. .. The contents of this publication are presen , anforgnfo national Pued units. rposes , PN40nty. strued as warranties or guarantees, express or implied, re ' or improve the designs or specifications of such product at any time without notice. y and while eve Cashco, Inc. does not assume responsibility for the selection, use or maintenance of an gar Ing the products or services described herein or their use or applicability. ry effort has been made s ensure their accuracy, they are not to be con- Cashco, Inc. product remains solely with the purchaser,We y product, Responsibility for proper selection, use and maintenance the hof any t to modify y6 SL R-q-TQ - it control number overrides remaining selections. �2/07/2� An "X" in POS 12 followed by a 5- ig MODEL SLR-2 PRODUCT CODER Po6 Pos P06 ❑ POS POS Ej —'--1011131— ❑ 5 ` ❑ ❑ MATERIAL 3 ❑ SEAL &SEAT DIAPHRAGM, 2 ❑ OSITION 6 & 7 is Seal ® ❑ P DYnam i static Seal POSITION 5 - BODY ?VER DOME MATERIALS Opt-81 Select CS, LCC or 551 her Material except in Canada, use SST. Cashco do Brasil, Lida, Cashco, Inc. Cashco GmbH AI.Venus, 340 PC Box 6 Handwerkerstrasse 15 Indaiatuba - Sao Paulo, Brazil Ellsworth, KS 67439-0006 15366 Hoppegaden, Germany PH +55 11 99677 7177 PH (785) 472-4461 PH +49 3342 30968 0 Fax. No. Fax. # (785) 472-3539 Fax. No. +49 3342 30968 29 www.cashco.com �cashco.com email: braziMcashco.com www.cashco.com v,rww': gero.com 17 email: sales@cashco.com email: germany Printed in U.S.A. SLR-2-TB ci R-2-TB DATA SHEET - OZONE DESTRUCT UNIT PROJECT NAME: OZONE DESTRUCT UNIT Tag No. Equipment Type and Model No. Number of Ozone Destruct Units Installed Model Number Type of Destruct Unit Equipment Rating and Capacity Off -gas Flow Rating Blower Size Blower Static Pressure Heater Size Temperature Rise Across Heater Design Inlet Ozone Concentration Design Outlet Ozone Concentration Destruct Catalyst Specification Sizing Criteria for Catalyst Proposed Approach for controlling vacuum in Contact Chambers Oshkosh Water Filtration Plant Oshkosh, WI M4500-1, M4600-2, M4600-3 Three (3) Size 2 Thermal/Catalytic Design Flow Rating up to 66 SCFM 2hp(max 3hp) Up to 24 in H2O 1.0 - 1.2 KW 30 - 45 OF 1 .5% <_ 0.08 ppmv Carulite 200 - 4x8 mesh (see attached Carulite Data sheet and SDS sheet Ozonia uses a proprietary calculation tool that takes into account inlet off - gas ozone concentration, off -gas flow rate, flow variation, sselcity), GHSV (Gas Hourly Space linear velocity across the catalyst bed, and exit ozone concentration to determine the required amount of catalyst. The calculation shows the required amount of catalyst to be - 70 Ibs. There is a variable speed drive on the of -gas blower that controls the vacuum based on the PIT in each contact chamber off -gas line 1 of 3 CHOKED: TITLE: PRELIMINARY Ozone Destruct Unit S eD GfNCa IOnS o. VEOLIA Water Technologies A 17xxx-06-0100 RE APPROVED: « c 600 WILLOW TREE ROAD LEONIA, NJ 07605 DATA SHEET — OZONE DESTRUCT UNIT PROJECT NAME: Flow Turndown Capability Data Sheet for Off -gas Blower Blower Motor Rating Blower Capacity Blower Manufacturer Model no. Material of Construction Pre -heater Rating Pre -heater KW rating 92 U Pre -heater sizing F Manufacturer �o Material of Construction a$� c o a 0"2 o13E � Total Connected Power a.o y E �Qoz Installed Power C y N Q© Miscellaneous Design Information Dimensions Skid Weight PRELIMINARY I I - I Lt I Oshkosh Water Filtration Plant Oshkosh, Wl SUEZ includes an automatic air inlet valve to allows a set amount of room air to enter into the destruct unit before the pre -heater to allow for operation as low as 100 Ibs/day 03 Production. (see attached cut -sheet) 2 hp (max. 3 hp) 1.2 bhp (at cold start) 66 SCFM at — 22 in. W C Cincinnati Fan HP-4A18 or NY Blower Size 2 Blower wheel and housing 31 S6 S (see attached cut -sheet) 1.2 KW AT = — 30 — 45 OF Heatrex Housing 316 S.S. Elements 316 S.S> 480V, 3 Ph, 60 hz, 20 Amps L 74 in. W 67 in. H 76 in. (not including silencer) 1850 Ibs. operating Ozone Destruct Unit S ecifications 2 o APPROVED: 2 Of 3 VEOL/A Water Te chno/ogles DWG No. 600 WILLOW I ,LOWOTfi E ROAD /� REV: 1 17xxx-06-0100 _ DATA SHEET — OZONE DESTRUCT UNIT PROJECT NAME: I Oshkosh Water Filtration Plant Oshkosh, WI Connection Sizes I Inlet 3" flange Outlet 3" flange Note: Field piping can be smaller based on actual flow conditions CHCKED: TITLE: PRELIMINARY Ozone Destruct Unit S ecifications DWG No. (� APPROVED: VEOLIA Water Technologles A 17xxx-06-0 1 00 L' 600 WILLOW TREE ROAD LEONIA, NJ 07605 BHT: 3of3 ... ..�� \w!\\\\\....�....... ... ° o ) T \(\}!\ :} ] „ . ';:°°r \ \- - § !(§!• - , .l f � § A\ ` ! M ��\.\ � �---------�. i � 00 ........ ....., ( .__ f / � � � L ` Q3S --- ( .__ f / � � � L ` Q3S --- Q G m �m 07 'i®m iD a m Ip II � U m co CARULITE®200 Granular Catalyst EC- SAFETY DATA SHEET according to Regulation (EC) Ns 1907/ of the European Parliament and of the Council, of 18 December 2006 ,q use concerning REACH 2O06 11 MATERIAL SAFETY DATA SHEET MSDS # CP-032 Pa e 1 of 6 Revision Date: July 2011 Supercedes: June 2009 Section 1 Chemical Product and Company Identification PRODUCT NAME: TRADE NAME: SYNONYMS: USES OF SUBSTANCE: COMPANY NAME CARUS CORPORATION -tiMULllE— 200 Granularlar C- a�st CARULITE® 200 Granular Catalyst None 200 Granular Catalyst is used for the destruction of ozone. COMPANY ADDRESS: INFORMATION: EMERGENCY TELEPHONE: Section 2 Hazards Identification 315 Fifth Street, Peru, IL 61354, USA (815) 223-1500 (Tel) (815) 224-6816 (FAX) !«vw.caruscorioration.com (Web) salesink, )caruscorporation.coin (Email) (800) 435 —6856 (USA) (815) 223-1500 (Other countries) (800) 424-9300 (CHEMTREC© USA) (703) 527-3887 (CHEMTREC® >, Other counh•i HAZARDOUS MATERIALS �INDENTIFICATION SYSTEMHelth Hazard (HMIS) RATINGS: Flanunability Hazard Reactivity Hazard 0 Personal Protection Index E NATIONAL FIRE PROTECTION ASSOCIATION 704 USA Health Hazard (USA) NFPA HAZARD — Materials which under fire conditions would give RATINGS: a ing combustion products Flaimnabifi than 1 hour exposure) Materials that on the skin could cause irritation. Hazar d 0 Materials that will not burn. (less Reactivity Hazard 0 = Materials which in themselves are normally stable, even under fire exposure conditions, and S ecial Hazard which are not reactive with water. EFFECTS OF ACUTE E None I. Eye Contact: EXPOSURE 2. Skin Contact: May cause eye irritation. May cause skin irritation or dehydrating of skin, 3. hilial Conn 4. Ingestion: May cause nose, throat and lung irritation. IrritaEFFECTS OF CHRONICting to illouth, EXPOSURE tluoat and stomach. Prolonged inhalation of manganese compounds above the TLV-TVV disorders. The sym toms simulate Parkinson's disease. A may cause lung irritation or central nervous system CARCINOGENICITY NTP; not listed. lARC Monographs; not listed, MEDICAL CONDITIONS GENE OSHA Rea ulated Dust or fine owder ma further RALLY me 1iibbi arieT01D Belie' wo POSURE • not listed. CARULITE® 200 Granular Catalyst EC- SAFETY DATA SHEET according to Regulation (EC)Ns1907/2006 of the European Parliament and of the Council, of 18 December 2006 concerning REACH Page 2 of 6 cA.rzus° MATERIAL SAFETY DATA SHEET Section 3 Composition and Information on Hazardous ingredients Mat_ material CAS No= EINECS No. % Hazar — ---� a -� *�** 5 mg Mn per cubic meter of air 215-202-6 40-70 PE, C 0.2 mg Mn per cubic meter of air Qanese Dioxide 1313-13-9 TLV-TWA*** Manb 131I5- 40 PEL** 1 mg Cu Per cubic meter of air 7-38-0 215-269-1 TLV-TWA""' y** ln1g Cu per cubic meter of air Copper Oxide Chemical Abstract Service Number copper dusts and mists (as Cu), 29 CFR OSHA Permissible Exposure Limit, manganese compounds (as Mn), 19 10. 1000 Table Z-1. Hygienist', 2005. TLV-TWA = the time we1gatedl ed expposed, day ge concentration T* American Conference of Govermnental a normal 8-hour workday and a 40-hour work week, to which nearly all workers may be rep rider any circumstances. without adverse effect. *x Ceiling Exposure Limit or maxinChemical l1e ti cal Substances concentration not to be exceeded European Inventory of Existing RISK PHRASES: 20/22 Harmful by inhalation and if swallowed. SAFETY PHRASES: 2 Keep out of the reach of children 25 Avoid contact with eyes Section 4 First Aid Measures EMERGENCY AND FIRST AID PROCEDURES lids apart to ensure flushing of the 1. Eyes Immediately flush eyes with large amounirrOfw on Pate e sr at istsleast 15 minutes holding entire surface. Seek medical atten tioll 2. Skin amounts of water. Remove contaminated clothing. Wash clothing before reuse. Flush contaminated areas with largeen. Seek medical attention. 3. Inhalation Remove person to fresh air. If breathing is difficult, administer oxy ive ►arge quantities of water. 4. Ingestion mouth to all unconscious or convulsing person. If conscious, g Never give anything by Do not induce vomiting. Seek medical attention CARULITE6200Granular Catalyst EC- SAFETY DATA SHEET according to Regulation (EC) Ns 19 of the European Parliament and of the Council, of 18 December 207/2006 concerning REACH 06 MATERIAL, SAFETY DATA SHEET Pa e 3 of 6 Section 5 Fire Fighting Measures The material itself is noncombustible but ma accelerate the burningof combustible mat FLASHPOINT None FLAMMABLE OR EXPLOS material. EXTINGUISHING MEDIA IVE LIMITS Lower: Nonflammable. Use extin uishin medium a ro riate for swlioundin maerials able. SPECIAL FIREFIGHTING PROCEDURES None UNUSUAL FIRE AND EXPLOSION HAZARDS other oxidizable substances. Keep away fi•om Beat and flanunamaterials. Shoulddnot be heated orrrubPotentially in contact with organic matter or conditions. an oxidizer under certain Section 6 Accidental Release Measures STEPS TO BE TAKEN IF MATERIAL IS Clean up spills immediately by scoo in CLEASED OR SPILLED with water. Cover loosely, Flush contaminated floors with abundant quantities of water ' p g ARULITE 200 Granular Catalyst into a metal drum. Deactivate by soaking federal, state, or local regulations. into sewer, ifpeimitted by Section 7 Handling and Storage Store in a cool, dry area in closed container. Segregate Phrotect containers against sical damage from easily oxidizable materials, peroxides, chlorates, and acids. Section 8 Exposure Controls and Personal Protection VENTILATION REQUIREMENTS Provide suicient mechanical and/or local exhaust to maintain ex osure levels below TL - RESPIRATORY PROTECTION V TWA limit for man anew. In cases where high dust exposure ma} exist, the use of NIOSH-MSHA dust and mist res ' res irator is advised. Engineering or administrative controls should be im lemented to cons EYE PROTECTION puator or an air -supplied Primacy eye prote't;�„ i� c col dust. GLOVES - "" y Biasses or; Rubber or plastic gloves should be worn. OTHER PROTECTIVE EQUIPMENT Normal work clotbing is sufficient. Section 9 Physical and Chemical Properties BOILING POINT, 760 mm Hg Not applicable SOLUBILITY IN WATER % BY SOLUTION VAPOR P BULK DENSIT17 A RESSURE (mm H) Not applicable p roximately 0.9 g/cc Insoluble MELTING POINT Starts to decom ose with evolution of oxygen at 704°C (LATI PERCENT VOLATILE BY VOLUME Not volatile APPEARANCE AND ODOR Black granulated solid; odorless. CARULITE@ 200 Granular Catalyst SHEET according to Regulation (EC) Ns 1907/2006 EC- SAFETY DATA European Parliament and of the Council, of 18 December 2006 of the Euro BEACH concerning pace 4 of 6 c.Aaus� MATERIAL SAFETY DATA SHEET Section 10 Stability and Reactivity Stable under normal condition1C0Moisture le materials o heat (704°C�1300°o e1lt reaction under certain STABILITYe cata cause vt CONDITIONS TO AVOID Contact with a peroxide and chlorates may especially organic solvents. May Quite organic material, esp Y INCOMPATIBLE MATERIALS Contact iction. May wit t p Tides in contact with acetylene. conditions, such as elevated temperature or form unstable acety initiate of merization of monomers. May IBUTTO HAZARDOUS POLYMERIZATION Not known to of merize. HAZARDOUS DECOMPOSITION PRODUCTS None CONDITIONS O Section 11 Toxicological Information Fnervous t diagnosed cases of manganese toxicity in humans have been reported following long-term exposures to airborne entrations of manganese abo ve the TLV-TWA. The usual form of chronic manganese toxicity involves the cents system. orts of adverse effects in hwnans from ingestion of manganese are rare. Section 12 Ecological Information tes ----- but exist in air as suspended particulate matter, which Fire ganese compounds have negligible vapor p' e influence of gravity.of the forth present. Insoluble forms, such as manganese t of manganese in water isinfluenced by the solubilityransported as sedimentsto be significant. mulation cf manganese in the food chain does not appear Section 13 Disposal Considerations Dispose of deactivated t chemical waste, after verifying that it is not ® 200 Granular Catalyst is not considered to accept us ante under 40 CFR 261. Dtsp r ULaminated with hazardous substances through usage. Section 14 Transport Information USA land D.O.T.) European Labeling in accordance Road/Rail Transport (ADR/RID) European Labeling in accordance with EC directive (Water, I•M.O.) European Labeling in accordance with EC directive (Air, LC.A.O.) Proper Name: ID Number: proper Shipping Name.' ID Number: Proper Shipping Name: I D Number: oper Shipping Name: Number: Manganese dioxide compound Not regulated Manganese dioxide compow1d Not regulated ound Manganese dioxide comp Not regulated Manganese dioxide compound Not regulated CARULITE® 200 Granular Catalyst EC- SAFETY DATA SHEET accordingto Regulation y Of the European Parliament and of the Council, ill, 18De C () Ns 1907/2006 g=^ Ft u s concerning REACH December 2006 MATERIAL, SAFETY DATA SHEET Section 15 Regulatory Information Pa e 5 of 6 US Federa7Re ulations TSCA:Allcomponn this product are listed on the TSCA inventory, Health & Safety Reporting List: None of the chemicals in this Product are on the Health & Safety ReportingList. Chemical Test Rules: None of the chemicals in this product are under a Chemical Test Rule. Section 12b: None of the chemicals in this product are listed under TSCA Section TSCA Significant New Use Rule: 12b, None of the chemicals in this product have a TSCA. CERCLA Hazardous Substances and correspondingSNUB underCA, er TS None of the chemicals in this product have an RQ, SARA Section 302 Extremely Hazardous Substances: None of tile chemicals ill this product have a TPQ, SARA Codes: CAS # 1313-13-9 and 1317-38-0; acute SARA Section 313: CARULITE' 200 Granular Catalyst contains manganese compounds WAS Re Reg, No. N/A) as part of the mixture and is subject to the reporting Clean Air Act: g of SectN/Aion and copper compounds (CAS This material does not contain any hazardous air pollutants, p a requirements of Section 313, This material does not contain any Class 1 or Class 2 Ozone depletors. Clean Water Act: None of the chemicals in this product are listed as Hazardous Substances under t None of the chemicals in this product are listed as Priori None of the chemicals in this product are listed as Toxic Pollutants under the CkIre CWA, OSHA: t3 Pollutants under the CWA• None of the chemicals in this product are considered highly hazardoust A State: by OSHA. CAS # 1313-13-9 is on the state lists fi•om NJ. FIFRA: CAS# 1317-38-0 is found. California Prop 65: California No Significant Risk Level: None of the chemicals in this product ar Euro ean/International Re ulations e listed. European Labeling in Accordance with EC Directives: HAZARD SYMBOLS: XnHarmful I RISK PHRASES: 20/22 Harmful by inhalation and if swallowed. SAFETY PHRASES: 2 Keep out of the reach of children 25 Avoid contact with eyes CARULITE® 200 Granular Catalyst EC- SAFETY DATA SHEET according to Regulation (EC) Ns 1907/2006 European Parliament and of the Council, of 18 December 2006 of theEACH concerning Pa e 6 of 6 c,AFzus° MATERIAL SAFETY DATA SHEET WGK (Water Danger/Prot 1 rand KBwS-Besch11uss (3) CAS# 1317-38-0: Vww5 ( ) Canada - DSL/NDSL: CAS # 1313-13-9 and 1317-38-0 are listed on Canada's DS as hazardous in accordance with the hazard criteria of the Canada — W HMIS: None of the components egulation product could be classified Cs. ontrolled Products Canadian Ingredient Disclosure List: Man auese and copper compounds are listed on the Canadian Ingredient Disclosure Ltst. g Japan Chemical inventory List MET an's METI List. CAS # 1313-13-9 and 1317-38- are listed S Jap Australia Chemical Inventory t C AICS List. CAS 4 1313-13-9 and 1317-38-0 are listed on An r List — IECSC CAS # 1313-13-9 and 1317-38-0 are listed on China's IECSC List' China Chemical inventory Section 16 Other Information Jul 2011 Chithambarathanu Pillai (S.O.F. n is accurate to the best of our knowledge. However, data, safety standards and satisfy theluselves that they The information contained herein to change and, therefore, holders and users should . CARUS CORPORATION government regulations are subs CI' OR THE are aware of all current data and regulations relevant to their particular use of product CORPORATION MAKES NO WARRANTY, EITHER DISCLAIM S ALL LIABILITY FOR RELIANC SON THE COMPLETENESS OR ACES INFORMATION INCLUDED HEREIN. CARD ANY WARRANT EMPRESS OR IMPLIED, INCLUDING, BUT NOT LIMITED TO, r oduct are beyond the control MERCHANTIABILIT Y OR FITNESS FOR PARTICULAR SE R PURPOSE se e p THE PRODUCT DESCRIBED HEREIN. All conditions relating to storage, handling, of Carus Corporation, and shall be the sole resp onsibility of the holder or user of the product. PERU, ILLINOIS 61354 CARUS CORPORATION, 315 5" STREET, L Carus and Desigred trademark of Carus Corporation. service mark Carus Corporation. soar CARULITE' is a registerri Irt 1998. Responsible Care' registered trademark of Cates Corporation. CoP) ' g '�ESPoNSIBLE rCARE and CHEMTREC� are registered service marks of the America" Chemistry our COMMITW N Council. CLOSED LOOP COOLING WATER SYSTEM Oshkosh Water Filtration Plant PROJECT NAME: Oshkosh, WI CW SYSTEM CLOSED -LOOP 1. Data Sheet on CW System Skids 3 0pen-loop Three () — Number of Cooling Water Systems Installed Skid -mounted Closed Loop, Type of Cooling System Centrifugal End Suction Type of Cooling Water Pumps Goulds Make/Model Number of Pump Model 3196 of Closed -Loop Cooling Three (3) Number Water Pump 5 hp motor (3.0 bHp) Size of Pump @ 70 ft head 90 gpm Rating of Pump �48inLx�30inWx48inHT Approximate Skid Dimensions Materials of Construction Cooling Water Pump compliant) Steel (to be NSF comp Stainless o Q Pump Casing Stainless Steel Impeller (3) —Closed-loop Skids N of Cooling Water Sy stems Three C � C @ao a Number Installed Skid -mounted Closed Loop, a R. � E System Type of Cooling Y Centrifugal "¢ �ar `aos Type of Cooling Water Pumps End Suction Goulds mLa Make/Model Number of PUMP Model 3196 Z N L `� ° Tree (3) h 3�°3C of Closed -Loop Cooling Number Water Pump 5 hp motor (3.5 bHp) Size of Pump cHCKEDTITLE: Water PUM s closed Coolin DWG NO PRELIMINARY PRELM: x-01 OO VEOLIA Water Techn-"9"' A17xxx-x APPROVED: LE0N1'A' o NJT ree a 07605 d 1 of 3 PROJECT NAME: Oshkosh Water Filtration Rating of Pump Plant Oshkosh, Wl Skid Dimensions 90 gpm @ 81 ft head Materials of Construction � —78inLx 54inWx64inHT Cooling Water Pump Pump Casing Impeller Stainless Steel (to be NSF compliant) Stainless Steel Type of Heat Exchanger Plate and Frame Make and Model No. of Heat Exchanger Polaris Model S20A-IG 16-54-TKTL73 Number of Heat Exchangers Three (3) Rating of Heat Exchanger Water Flow 348,850 BTU/hr Hot Side Cold Side 88 gpm Max. 90 gpm Water Temperature Hot Side Inlet/Outlet Cold Side Inlet/Outlet 97 OF / 89 of a Q I�-p Pressure Drop 860F / 94 OF �o Hot Side a a�a maa c o 0 Cold Side s 5.0 psig �_� a _o Heat Exchanger Design s 5.0 psig N N Q ~' Pressure 150 psig Pressure Vessel Code ro��0 z� Q© Dimensions — Heat E xchanger ASME Materials of Construction (see attached drawing) Heat Exchanger Plates 316 S.S. Frame Ductile Iron CHCKED: TITLE: PRELIMINARY Closed-Loo APPROVED: lro CSHT: o olin Water Pum VEOLIA Water Technotogtes T DWG No. S 2 of 3 LEONIA'NJ07605 sd A REV: 17xxx-xx-0100 - PROJECT NAME: 2 Sizing Criteria for Expansion Tanks 3, Sizing Criteria for Air Separator Tank 4. Sizing Criteria for Chemical Pot feeder Oshkosh WaterFiltration t non Plant Oshkosh, Veolia has a sizing program that to stem into account liquid volume HIE he sy including, 03 Gen, PSU, Separator, skid piping and field piping along with the min/max Ca expected tes temperatures The program gtank acceptance the system expansion, Tank volume volume and total Expansion required Taco has literature that looks pressure overall flow rate and required drop to provide a max. required tank volume that can differ of e water a d Without a strainer as pa oop Veolia has a sizing program that takes into account the overall watervolume looploop and the closed loop cooling required concentration of biocide, corrosion inhibitor Chemdetermine Pot feederhe size of the standard for Heat 5. Data sheets Exchanger Plate Arrangement 6. closed -loop CW 7. Required quality 0 €� Scale inhibitor, 8. Recommended inhibitor o biocide and corrosion = ay°a 0 c g. List of Spare Part =QOZ o,�mo C C NON iU NL Q© L m = p 10. GA Drawings (see attached) (see attached) (see attached) There are wide variety of chemicals available as a corrosion inhibitor and biocide 1. Two sets open loop cooling water pump bearing kits. cooling water pump 2. Two sets closed loop bearing kits. 3. Three gaskets for heat exchangers. (see attached) TITLE: COOlIn CHOKED: Closed-LOO V Ww PRELIMINARY VEOLIA Water Technologies APPROVED: ' LEOWA. NJT r07605ad Water PUm s 3of3 DWCi ivu. q 17xxx-xx-0100 WD J 7 o D - Q Nam z - � a � z W 1 w � C? Z O Q n LL O Z X < X � W_ > O U w at Qi ,9ybse 3 w_ w J c � I H Model 3196 MTi OUTLINE DRAWING Size 1.5x3-10 _. ..__ -- C"' n-T €rand 16,00 43,25 3.75 23,50 Discharge Coupling 8,50 guard 1 scum suction $:25 y 12.44 .a375 I — .{ 0,75 I 1-0,15 in, dia. holes 1,25 - 42.50 45,00 ITT I � � 20,94 I tT ! _ I 4.5G 4,50 +1 12.00 Weights and Measuivinents 0 5 Notes and Re ei,ences MTR DIMENSIONS ARE APPROXIMATE INSTALL FOUNDATION BOLTS IN PIPE SLEEVES ALLOW FROM 0.75 to 1.501n. FOR THE BASEPLATE IS DESIGNEDTHERV FOR GROUT INSTALTHE INSTA OAT ON MANOUAL INSTRUC7010NS.TED REFER TO Tolerance is -0.38 +0.38 Foundation bolt grip thickness FOR PUMP TAPPED OPENINGS REFER TO DWG•: TAF230241001 -� DRAWING IS FOR REFERENCE ONLY, NOT CERTIFIED FOR CONSTRUCTION UNLESS SIGNED. Customer: VEOLIA WATER TECHNOLOGIES Serial No: Customer P.O. No. Offer) Item No: 001 End User: Oshkosh en Loop Cooling Water Pumps Service: Op :Gpyrigttt 2:02 ITT Carts All dimensions are in inches. Drawing is not to scale DRAWING NO AF23024/001 page 5of13 Weiahts (Ibs) are approximate Model:3196 Size:1.5x3-10 Group: MTi �601lz RPM:1750 Stages:1 Job/Inq. No. Purchaser: VEOLIA WATER TECHNOLOGIES End User: Oshkosh WI Item/Equip. No.: 001 (Base Offer) Issued by: Angela Fisch Service : Open Loop Cooling Water Pumps Quotation No.: AF23024 Rev.: 0 Order No.: Date : 10/11/2023 operating Conditions Certified By: Liquid: Temp.: Potable Water Published Efficiency: Pump Performance S.G./Visc.: 86.0 deg F 1.000/1.000 cp Rated Pump Efficiency: 56.5 % 52 5 % Suction Specific S peed: 10,432 gpm(US) ft Flow: 90.0 gpm Rated Total Power: 3.0 hp Min. Hydraulic Flow: 11.5 gpm TDH: 70.0 ft Non -Overloading Power: 4 2 hp Min. Thermal Flow: N/A NPSHa: Imp. Dia. First 1 St g(s) 8.4375 in Solid size: NPSHr: 2.0 ft Vapor P Max. Solids Size: 0.2190 in Shut off Head: 01 75.5 ft ress. Notes: 1. Curve shown is at ambient temperature conditions. CENTRIFUGAL LNG OULDS PUMP CHARACTERISTICS Performance Standard: HI 14.8 16 basis Powar' tYl ft 140 40 120-.._... 30 100 80 20 60 1 40 bin kW 1. 1 e Susp. Solids (by wtg): I on CDs 5021-2 1750 ___ 3196(HT3196 1.5X3-10 0 20 40 60 80 0 10, 15 20 100 25 120 140 160 30 35 Viscosity corrections have been performed in accordance with HI 9.6.7-2015 Due to the low power (<10kw/13hp per HI 14.6, head: +/- goo, paragraph 14.6.3.4.1), acceptance tolerances are rate of flow: 10% PUMP total ITT Nuo—MU-1pD55OUTLINE DRAWING s:3i7raa11 ------------------------ -- 43,25 23,50 3.75 Model 3196 MTi c:_^ 4 AY3-10 4,00 �— Discharge 6.75--t -' 6.$8 Co i r_ T I 8.50 guardrd ( M94 gu I �—^ Suction � y � 8.25 13,19 12.44 0.15 4,50 �1 4-0.75 in, di a, holes . {I 1.25 d.SQ .----�I 1 �.00 45,00 C All dimensions are in inches. Drawing is not to scale Weights (lbs) are apprOXima ITT Weights and Measurements 0505�_ 4 851b Lh 3 66.5 Notes and Refer°ences - MTR DIMENSIONS ARE APPROXIMATE INSTALL FOUNDATION BOLTS IN PIPE SLEEVES ALLOW FROM 0.75 to 1.50in. FOR THE BASEPLATE IS DESIGNED FOR GROUT NOTED.RVIASE I S LLAT10NSTALLAT NN MANOUAL INSTRUCTIONS REFER TO ' Tolerance is -0,38 +0.38 " Foundation bolt grip thickness FOR PUMP TAPPED OPENINGS REFER TO DWG.: TAF23024I002 DRAWING IS t-urc Mc ' -NCE ONLY. NOT CERTIFIED FOR CONSTRUCTION UNLESS SIGNED. Customer: VEOLIA WATER TECHNOLOGIES Serial No: Customer P.O. No: Offer) Item No: 002 cod/UeeC Closed Loop Cr: Oshkosh WI ooling Water PUMPS DRAW —NO AIAF23024/002 11iyright 202- ITT corp , Page 110f13 Model:3196 Size:1.5x3-10 Group: MTi 60Hz RPM: 1750 Stages:1 Job/Inq.No. Purchaser: VEOLIA WATER TECHNOLOGIES End User: Oshkosh W► Item/Equip. No.: 002 (Base Offer) Issued by: Angela Fisch Service: Closed Loop Cooling Water Pumps Quotation No.: AF23024 Rev.: 0 Order No.: Date : 10/11/2023 Operating Conditions Certified By: Liquid: Potable Water Pump Performance Temp.: Published Efficiency: 56.0 % 86.0 deg F Rated PumpSuction Specific Speed: 10,432 S.G./Visc.: 1.000/1.000 c Efficiency: 52.5 % gpm(US) ft Flow: p Rated Total Power: Min. Hydraulic Flow: 90.0 gpm 3.5 hp 12.4 gpm TDH: Non -Overloading Power: 4,8 hp Min. Thermal Flow: N/A 81.0 ft Imp. Dia. First 1 St NPSHa: 9(s)9.0000 in Solid size: NPSHr; Max. Solids Size: 2.0 ft Shut off Head: Vapor Press: 0.2190 in % p Solid (by � s Sus 85.9 ft Notes: I. Curve shown is at ambient temperature conditions. g): g CENTRIFUGAL PUMP CHARACTERISTICS Based on Cp3 �� �I.i�.PUMPS Performance standard: lit 14.6 1 B basis power, RPM 1750 5021-2 n'i ft Model 31961HT3196 Sfze; 1.5X316 160 _ - - - %Q 40 140 - $0 120- -- -. � 70 ._�__ 30 100 101 - - _ .... Eff w., 60 80 20 - 50 60 - _- -40 1 40 gin ein -- 30 20 - . _. _ -20 10 kW 4. m ft 1,2 NP Hr _ Po f 1. 0.8 2 0 . 0, 4 0 20 40 60 80 1 5 10 15 20 100 25 120 140 160 gpm - 0 0 30 m°/h Viscosity corrections have been performed in accordance with HI 9.6.7-2015 'Due to the low power (<10kw/13hp per HI 14.6, head: +/_ g% paragraph 14.6.3.4.1), acceptance tolerances are rate of now: 10o �o, pump total I'TT 12 Page 1 of 2 Classified as Business Classified as Business m LU 0: Q 0 WJ _ C1 W J m , F < z W J' H W h 0 a z m a W Q H: N _J 0 LL J O Z u Q W u H w J l7 M � � E M (�� a , F F O O z z - O N U S _ fs ,z - m ° t � � o V r �n� :OR MARINE USES Kchangers are well adapted to including; ► Fresh -Water Generator ► Engine Jacket Cooling ► Lube Oil Cooling Utilizing the heat from diesel engine jacket cooling water, the POLARIS Fresh Water Generator evaporates seawater to produce pure drinking water. Contact us for details on the engineering and applications of POLARIS Fresh Water Distillers. Seawater filters can also be installed in the plate heat exchanger. This is useful for Plate heat exchangers used not only on shipboard, but also in offshore platforms. The filter catches smaller particles, resulting in longer intervals between service and maintenance. Polaris Plate Heat Exchangers www.polalisphe.com lnfo@n�j.,;. rp of a plate heat exchanger An ato y carrying Bar Plate Pack Plate Connectior He; Flange Connect Foundation FRAME late A strong, rigid, durable frame is the foundation of any p heat exchanger. POLARIS frames are ASME Secesigned . Div.loo prevailing national codes. They construction standards, and are also designed to streamline assembly, service and A large rover 11 to forth, so it's easy to open and close a PO service and maintenance. Optional inspection holes allow convenient examination of the plate pack interior —useful ain pulp or fiber, which can cause clogging. when media cont polaris plate Heat Exchangers www.p.larlsphe.com info@polarlsphe.com �! s11J�,l1 r�j'ifirff( ANATOMY OF A PLATE HEAT EXCHANGER continued HEAD Standard POLARIS PHEs are single -pass units with all connections on the head. This configuration simplifies service and maintenance —no need to dismantle the pipe work to access the interior. The head and the column can be equipped with strong foundation feet that make it easy to secure the heat exchanger. This design also makes future plate pack expansion much easier. PLATE PACK The heart of each POLARIS PHE is the plate pack, where heat transfer takes place. The pack is formed by Plates featuring state-of-the-art Plate pattern design. Each plate is fitted with a high -quality gasket to seal the heat exchanger, guide the flow, and align the plate. Combining POLARIS plate types and patterns delivers best PHE efficiency for the thermal requirement of the application. CONNECTIONS Connections in Polaris gasketed PHEs range from 1 " to 26". Threaded pipes and flange connections designed according to all applicable standards eliminate the need for reducers in the piping system. To guard against corrosion, flange connections may be lined with rubber or clad in the same material the plates are made from, such as AISI 316 or titanium. TIE BOLTS To cut labor effort and assembly time, tie bolts are made to be tightened from the head side of the heat exchanger. This simplifies opening, closing, and tightening the heat exchanger. �HKKYING BARS Strong and durable, our carrying bars prevent distortion or slumping from the weight of the plate pack through years of operation. Plates slide easily along is lo enough to make room to clean the Plates wltho tl ch removig them from the frame. Also, the carrying enables extraction of one plate while I ab ng the ortherses in place. GUIDING BARS POLARIS' properly designed guiding bar helps prevent misalignment of the plate Pack, properly supporting Plates during assembly and when the PHE is opened for service. It's strong enough to withstand the side load of powerful tightening forces exerted when the heat exchanger is assembled. Polaris Plate Heat Exchangers www.polarisphe.com info@polarisphe.com j. j„rj s f;11lFf�> Plates Hanging system inlets Drain Zone Distribution Are; Heat Transmission Are and Main Pattern Art Gasl Traditional Plate The variety of our plates is key to our ability to deliver the so many industrial applications. The many pressing P and angles of our plates enable Polaris PHEs to supply optimum solutions wherever they're installed. 1304/316 or titanium, but Most plates are made of AIS materials, depending n also be made from other p HEAT TRANSMISSION AREA Our many years of experience in thermal design and plate atest strength. Designs pressing techniques is our gresibased area a on this knowledge maximize the heat transmis each plate, and improve the thermal efficiency of the entitre process knowledge enables us to develop heat pack. Our p perfectlymatch your requirements, transmission areas that Imized for maximum efficiency. delivering a plate size op Free-FIoW Plate Semi -Welded Plate on media and temperatures. Plates form the plate pack, ween the head and the follower which is held firmly bet, eliminate of the frame. corrugated patterns en in the entire heat transmission area, helping "dead zones." DISTRIBUTION AREA The distribution area on POLARIS plates features angled guiding channels that ensure an even distribution n She media across the entire plate, preventing "dead Pressure drop in the distribution area is minimal. It's used in the heat transmission area instead, for better heat transmission. o,.1aris Plate Heat Exchangers www.polarisphe.com Info@polarisphe.com ss lh", `r %f tj'f e �sf �; jJf�fjf olaris Safety -Pair Double -Wall Plates Ultimate Safety in a Leakage Protection System POLARIS Safety -Pair —Detect Leaks Before They Cause Double -Wall plates are Damage. the ultimate safety measure for PHEs. Even in the unlikely event plates are damaged, the system eliminates the risk of mixing the media used in the heat exchanger. This is especially important where mixing of media could cause environmental hazards or serious equipment damage, Amhad LEAKAGE DETECTION The "double plate" system makes any leakage visible from outside the PHE. Leaks caused by corrosion damage or plate cracks enable maintenance Personnel to quickly identify malfunctioning plates, and the heat exchanger can be taken out of service for repair. Because any leaks are external instead of internal, the media will never combine. This makes Safety -pair Double the ideal solution when Wall Plates the heat exchangers utilize media that must not be allowed to mix. u uin zone. Safety -Pair Double -Wall plates i RMN Warm Media Cold Media ;Leakage Media Flow - > ; -if uouole-wall plate. The 'double plate"inlets are welded together. Polaris Plate Heat Exchangers www.polarisphe.com info@polarisphe.com SUPPEMENTAL NITROGEN SYSTEM PROJECT NAME: 1. Data Sheet Equipment Type and Model No, Number of Nitrogen Generation Systems Installed Type of Nitrogen System Compressor Manufacturer & Model Number Type of Compressor No. of Compressors Dryer Manufacturer & Model Number Type of Air Dryers Equipment Rating and Capacity Compressor Rating Nitrogen Feed Rate Flow Control Method Dryer Rating Outlet Dewpoint Input Power Air Receiver Tank Volume, Rating Physical Dimensions Dimensions — Complete Unit Oshkosh Water Filtration Plant Oshkosh, Wl One (1) Compressed Air Dryer System Quincy QOF-5 Oil -free Rotary Scroll Two (2) Quincy QMOD-0008 Heatless Dual -tower Desiccant Dryers 7.95 scfm @ 116 psig 1.0 — 2.3% by weight 1.47 — 3.63 scfm Sierra or equal Mass Flow Controller 6.0 scfm inlet flow — 3.9 scfm outlet required (max.) @ 1200 Ibs/day, 10% 03 < -90 OF 480V, 3 Ph, 60 Hz, 15 amps 80 gallons, ASME code stamped 116" L x 55" W x 78" HT PRELIMINARY IITLE: Nitro en Generation S stem S l o APPROVED: eCIfICatIOnS � of 2 F � � A VEOLIA Water Teohnotogtes DWG No, LE WILLOW TREE ROAD A 14xxx-10-0600 REV: - LEONIA, NJ 07605 SUPPEMENTAL NITROGEN SYSTEM PROJECT NAME: Weight — Complete Unit Connection Sizes - Materials of Construction Air Compressor Air Dryer Control Panel Skid 2. Dimensional Drawings Oshkosh Water Filtration Plant Oshkosh, WI 2500 Ibs outlet Painted steel Painted steel Painted steel Painted steel (see attached) CHOKED: TITLE: Stem S ecifications PRELIMINARY Nitro en Generation S DNS No. VEOLIA Water TechnetOgles A 14xxx'-10�-0600 APPROVED: 600 WILLOW TREE ROAD 0,0 VeOLIA LEONIA, NJ 07605 2of2 r � o W w "' J N - S t-� Q lM 0 0 0 0 Cl) Rl pal -Free Compressors Quincy QOF Series I Oil -Free I Air Compressors I QOF 2.30 HP Quality Comes All Shapes UMM ""ul Just One Color Pure Oil -Free Air. As there is no metal -to -metal contact between the compression scrolls, there is no need for oil lubrication in the com chamber. Therefore, the scroll compressipression on principle guarantees high -quality, oil -free air. As a result, the ()OF compressor is oil -free in every way. Energy Efficiency. The QOF scroll compressors, standard equipped with IE3 Premium efficiency motors, are suited for sensitive applications which require flexibility and energy efficiency. Unloaded power consumption is eliminated thanks to the simple start/stop control. Advanced scroll technology guarantees an optimal free air delivery and low duty cycle applications. Extremely Low Noise Level. The slow speed of the scroll compression elements ensures that the QOF scroll compressors are extremely quiet. Sound levels are as low as 53 dB(a), making the QOF the sensitive working environment. perfect choice for Your Simplicity And Reliability. The QOF scroll compressors stand for simplicity and reliability. The compressor has a minimal number of moving parts, ensuring a long operating life with limited service interventions. With their integrated design, Quincy Compressor's QOF scroll compressors have a minimal footprint and offer easy serviceability, Proven Peace of Mind. Since 7924, Quincy Compressor has been leading the industry in cornpressed air technology, drawing on vast experience and continuous technological innovations. You can rest assured at all times: severe certification and testing ensure air is supplied to the highest standards of quality ont ol. to QO F 2.30 Oil -Free Series Oil -Free Compressors Industries such as pharmaceuticals, d textiles0 annotrbsk any chance of oil od and beverage, electronics contamination in their processes. Therefore, it is essential that the compressed air is 100%oil-fre o reeresendtsrd is the highest73-1 air purity. certification, in which Class Z p is the only way to ensure oil -free air for critical processes and your peace of mind. Outstanding reliability, low maintenance and operating costs make oil -free compressors a sound investment. Scroll Technology: How Does It Work? Air compression is achieved through the orbital motion of two spirals. One stationary, the second mobile, their interaction pulls the air into the compression chamber. In a regular and continuous way, the mobile spiral compresses the air through a reduction of the volume. The air flow is directed to the center of the spiral after which it is cooled. As the spirals never make any contact, this compression process does nos guaranre any tee lub icoil free Consequently, the QOF series compressors compressed air. Fixed scroll Cooling fan Orbiting scroll Suction chamber Fail-safe temperature sensor Suction opening Compression chamber A Delivery opening QOF 2.30 Oil-Free Series The Power of the Oil -Free Range The QOF 2-30 oil free scroll compressors provide high -quality air Omii:D for critical applications in a wide range of industries. The QOF 2-30 range also provides top class performance, premium efficiency and quality. Oil -free compressors also reduce your total cost of ownership in three ways: (1) allows you to avoid purchasing expensive filter replacements, (2) cutting maintenance costs for treating oil condensate and (3) extra energy costs are eliminate combat pressure drop across filters. Performance Pressure rating 116 to 145 PSI Output from 4 to 86.5 CFM Sound levels as low as 53 dBA Efficiency Built-in dryer to reduce downstream pressure drop (optional) Latest compression technology High -efficiency IE3 motor standard Quality • ISO 8573-1 Class Zero certified quality air • Corrosion resistant materials • Identification & logging of shutdowns • Service schedule adjustment • Extremely low vibration Class Zero: Eliminating Any Risk Class Zero represents the best air quality possible. In critical environments, it is essential that the compressed air is 100% oil - free. Contamination by even the smallest quantities of oil can cause costly production down time and product spoilage, resulting in product recalls and loss of reputation. � J.V One Package - Multiple Benefits The innovative features of the QOF 2-30 range provide you with maximized efficiency, excellent air quality and low noise levels. State -of -the -Art Element • Highly efficient profile • Robust, reliable design and easy access for service High Efficiency Motor urn motors standard • High efficiencylE3/NEMAPI em classF motor for heavy duty • Totally enclosedair-cooled operation Cool Canopy • Increased ventilation due to vertical design • Lower outlet temperatures • Oversized cooler improving performance • Improved canopy design: better dryer performance and easy access Optional Integrated Dryer • Integrated package reduces foot print, maintenance and installation cost point of +37°F • Designed to guarantee a constant pressure dew • Ensures delivery of dry high -quality air Options to Maximize Operations A wide range of options enables you to get the most out of your QOF compressor. Vertical design increases ventilation Integrated dryer reduces tootpnnt QOF.20 (4 Modules) Variable Air Delivery General Options (0.01' 2.7.5) QOF 2.30 Dimensional Technical Data • Tank -mounted solution • 70 gallon 26 33 .. � 30 � QOF 2-7.5 FM 26 33 Air Quality options (QOF 2.7.5) 40 QOF 2-7.5 FMD j 57 • Integrated refrigerant dryer 48 l z6 j 48 QOF 2-7.5 TM &TMD 30 67 QOF 10.15 FM & FMD 67 30 73 QOF 20-30 FM & FMD I `i TM Tan Mountl TMD =Tank Mount Dryer FM=Floor Mount FMD Floor Mount Dryer I 70 Gallon 70 Gallon j Control & Monitoring The QOF range comes with a wide variety of control and monitoring features that allows an increase in the compressor's efficiency and reliability. The QOF 2-7.5 compressors are equipped with gauge controls which automatically starts/stops the unit when the required working pressure is reached. A Graphic Controller is included in the QOF 10-30 series. Intelligent Graphic Controller QOF 10.30 The multiple control and monitoring features of the controller efficiency and reliability. Efficiency is maximized on the QOF 10-30 units dramatically increase the compressors by controlling the main drive motor and regulating the system pressure within a pre- defined and narrow pressure band. Warning indications Graphical indication service plan Integrated sequence for up to 6 compressors limiting the energy consumption and equalizing running hours across your whole system Online visualization of running conditions OF 2-30 Technical Data *weight based onnoormountedunits without integrated dryer ' NOTE: Shipping weights can vary based on unit configuration and packaging, Variable Air Delivery The QOF 10-30 units are equipped with multiple scroll modules, The units utilize Variable Air Delivery technology which controls the requested number of modules depending on your air demand. This technology allows the QOF 10-30 to be able to adjust to demand fluctuations. The intelligent controller prevents simultaneous start of the modules and ensures a very narrow pressure band is maintained. This optimizes the efficiency of the compressor and guarantees a very stable system pressure. oil -Free Systems Best practice Air compression is achieved through the orbital motion of two spirals. One stationary, the second mobile, their interactiond pulls the air into the compression chamber. In a regular continuous way, the mobile spiral compresses the air through to the a reduction of the voluit is tooted As theThe air flow is lspiralds never m ker of the spiral after which compression process does not require any lubrication. contact, this comp p guarantee 100%oil- Consequently, the QOF series compressors g by application The System requirements vary diagram below represents free compressed air• se t the best practice system nptallation for optimal clean air delivery to the point of use. *Qws ncu y .- - U.UI lvnu�n Quincy Oil -Free Compressor ling Receiver Bulk QPNC Non-Cyc 0.01 PPM 5 al/CFM QOF-5 Liquid QED Cycling DP5 g DP6 DP4 Quincy Oil -Free Compressor QOF-7.5 70,1 PPM DP7 *Qws wet meauu— F Quincy Oil -Free Compressor Receiver QMOD (Prefilter Included) Bulk QOF-20 Liquid lgal/CFM DP6 5gal/CFM *WSN recommended for non -dryer units only �Com resse ' p d Air Systems Best Practice Air Quality Classification ISO 8573.1 r td8'F; 4 8 e 0.01 1 +38°F; 4 Quincy Rotary Screw QWS Wet QMF Bulk Receiver = Refrigerated Air Dryer QCF 9 Liquid igal/CFM = 0 MppM OPNC Non -Cycling 0.01 Micron RecDry eiver DPI and/or QED Cycling 0.01 PPM 59al/CFM DP3 t Mist k DP4DPS QAF Eliminator,' 0,003 PPM DP2 Vapor & Odors ate. COTE: requires CX["f 2.001 Quincy Reciprocating AC OWS Moisture Separator QPF Particulate/Coarse Coalescer QMF STD 0.1 PPM Coalescer, 1 Micron QCF Polishing 0.01 PPM Coalescer CXNT Xtra 0.001 PPM Coalescer QAF Activated Carbon Absorber HTDT High Temperature, I Micron QPNC Non -Cycling Refrigerated Dryer QED Cycling Refrigerated Dryer OMOD Modular Heatless Dryer QDTS Small Heatless Dryer OHD Industrial Heatless Dryer QHP Heated Purge Dryer QBP Blower Purge Dryer QRHT High Temp. Refrigerated Dryer AC After Cooler DP Drain Point nu Quincy Conde nsate Purifier C uincy N,&I-ante You Demarld R.Iisbility Yau Trust, " s ° ® o y �1 BkS x` a QCF 0.01 Micron Desiccant Heatless Air Dryer QDTS—Small ry QMF Dry Liquid ; DP b j 0.01 PPM DP7 1 Micron Receiver QHD—Industrial Particulate Sgal/CFM -40T PDP e z fi a f # # J a # s # a # k # o QCF 0.01 Micron Desiccant Heated Air Dryer QMF 0.01 PPM QHP—Heated Purge QBP Blower Pure HTDT Dry Receiver DP8 -40'F PDP g I Micron 59al/CFM Particulate a E 8 QPF High Temperature/ $ QMF 5 Micron Refrigerated Air Dryer 1 Micron 5 PPM QRHT—High Temp. I PPM DP9 DP70 DP11 701 N. Dobson Avenue I Bay Minette, AL 36507 Phone 251.937.5900 1 Fax 251.937.0872 Email: infoCquincycompressor,com I QuincyCompressor.com QAF Q003 PPM Vapor & Odors UN, 100C FFMrop0 psi 8 F, 40 0 Removal Drain n Gallons Drain Gallons Drai--n Gallons QAF Point i Per Year Point 0,003 PPM 31 � per Year Point ; per Year Vapor& 2-2000 5 140i 9 30 Odors 3 305 3000 103- 4 1300 310 8 310 11 120 ©2017 Quincy Compressor. All rights reserved. Printed in U.S.A. (QOF•002 06117) k � J3 Blower , • Purge • Quincy desiccant air dryers purify compressed air by adsorbing water vapor. • Pressure dewpoints of -40°F to -100°F are attained by directing the flow of wet com- pressed air through a bed of highly adsorbent Q-Sorb desiccant. • "Q-Sorb" is an enhanced formula of activated alumina. It provides better uniformity, more efficient use of available surface area, less dusting, longer life and lower pressure drop. • Heatless dryers use a small portion of the dried compressed air to purge the off-line tower. • Heated Purge dryers use an even smaller portion of the dried compressed air combined with heat for regeneration. • Blower Purge dryers combine heat with forced ambient air for regeneration. • Optimum performance and energy efficiency are maintained by employing a selected integration of dedicated valves, unit specific electronic controls, monitoring devices, and demand controls. • 5 Year Warranty on all actuated switching valves. Flow Schematics • To regenerate the off-line tower, atmospheric dry purge airflows through the regenerating bed. • Purge air dries the moisture laden desiccant beads and is expelled to the atmosphere through the mufflers. • Moisture load, velocity, contact time and cycle time determine the amount of desiccant required, and the size of the vessels. • To ensure optimum moisture adsorption, velocities are kept below 50 feet per minute. The air is in contact with the desiccant for at least 4.5 seconds ensuring performance, while keeping a low pressure drop. QHP Heated Purge QHD Heatless .40°F to -100°F Dewpoint First Cost: Medium 40°F to •100°F Dewpoint Operating Cost: Low First Cost: Low Maintenance: Low Operating Cost: Medium to High Purge: 7% Maintenance: Low w/MBR Option: 3.5%Avg. Purge: 15% QHD Heatless Desiccant Dryer QBP Blower Purge +10°F to -40°F Dewpoint First Cost: High Operating Cost: Low Maintenance:Medium Purge:1.75% Avg. QHD/QBP 210-635 (Standard) Quincy offers a standard filter package for all desiccant dryer models 635 and below. Included in this package are two prefilters and an afterfilter to increase the quality of air going to your system. • Prefilters prevent oil contamination to increase desiccant life time. • An afterfilter protects the airnet from desiccant dust and network contamination. • Easy to assemble and maintain. No extra piping and filter connections are required. Package Filtration Pre Filter Model QCF • Type Polishing Coalescer • Rating 0.01 Micron The factory -selected coalescing prefilter is installed at the dryer inlet. The polishing QCF coalescing prefilter protects the dryer from liquid contamination and includes an electronic condensate drain with element condition indicator. The Aluminum filters feature a push - to -fit element connection design and color coded element end caps. The housings are electrophoretic coated and carry a 10-year warranty. Pre Filter Model (IMF • Type Standard/Particulate Coalescer • Rating 1 Micron This prefilter is designated to filter initial contamination up to 1 micron before going through a second phase of filtration to better protect the dryer. The housings of both prefilters are the same and interchangeable. After Filter Model QPF • Type Particulate • Rating 5 Micron To protect downstream equipment from the harmful effects of desiccant dust, Quincy has selected our high -efficiency QPF 5 micron particulate filter. Since the Q-Sorb produces so little dust, this afterfilter will have an extended life expectancy. The housings are configured the same as the prefilter and are interchangeable. SiAng Table 3.6 8 Simplex I 3,6 QMOD00008 3/8„ I 10 Simplex 11.1 QM 3/8" i Simplex 11.1 3.6 QMOD00015 3/8" 15 Simplex J 1.1 3,6 QNIOD00025 3/8" i 25 Simplex 11.1 3 3.6 QMOD00035 f 3/8" 35 Simplex 20.5 6,5 QMOD00045 3/4" 45 r Simplex 20.5 i 6.5 QMOD00055 € 3/4" 55 i Simplex 20.5 6.5 QMOD00065 3i4"' 65 Simplex 20.5 6.5 QMOD00085 [ q 1" 85 Simplex 20.5 6,5 I QMOD00105 1" 105 Simplex 3 20.5 6.5 QMOD00135 11/4" 135 E 175 Simplex 20,5 6,5 QMOD00175 11/4" Duplex 20.5 12.9 QMOD00215 1 1 /2 215 i Duplex 20,5 12.9 QMOD00275 11l2 275 Duplex i 20.5 12.9 ' QMOD00365 I s 11/2" 365 to the above flow rates to suit the application and ensure dryer performance. Note: The temperature and pressure correction 95,,F factors below should be applied at the dryer inlet. II flowrates are based on 100 psig and A o All units provided with prefilter and afterfilter. Standard Pressure Dewpoint Maximum Working Pressure Electronic Controls Minirnun Inlet Temperature Maximum Inlet Temperature Minimum Ambient Temperature Dryer Correction Factors Inlet PSIG 22.0 3 25.0 36 32.1 43 47.4 53 62.9 68 27.6 1 117 ' 31.5 130 35.4 141 43.3 165 55.5 201 63.4 225 79.1 271; 55.5 379 63.4 423 79.1 511 Capacity Required Capacity x Pressure Correction x Cap y 40°F Corrected Temperature Correction -100°F 175 x 1.25 x .93 58 PSIG 203 SCFM Dryer Required - Required Capacity /Pressure Correction/ 232 PSIG Temperature Correction DC, 100VAC - 240VAC 175/ 1.25 / .93 150 SCFM 35°F 122°F 41°F Dewpoint Confection Dewpoint(°F) Dewpoint correction factor ? 1'•0 0,7 Dryer Correction Factors 50 0.35 • ' 60 , 0.51 NA 0.56 70 NA0.65 0.65 80 ;' 0.77 NA 0.74 90 0.87 NA 0.83 100 0.97 NA 0.91 110 1.05 NA 1.0 120 ' 1.13 NA 1.09 130 1.2 NA 1.18 140 1.27 NA 1.27 150 1.33 NA 137 160 1.38 NA 1.43 170 NA 88 0. NA 180 ; NA 0.94 NA 190 NA 0,99 NA 200 j NA 1.05 NA 210 13 NA 1.11 NA 1.16 J i NA 90 3 1.0 an • ' ,, • 95 1.0 1.0 1.0 100 1 1.0 105 0.81 i 1.0 1.0 110 i 0.76 0.81 0.85 ` 115 0.67 0.76 0.74 120 0.58 ( 0.67 0.64 0.58 0.55 Q-Sorb Enhanced Desiccant Corrected Capacity = (Required Capacity) x (Pressure Correction)orre QU11 cy's exclusive Q Sorb desiccant is t11E x (Temperature Correction) first significant improvement in activatec 1000x 1.18x.74 alumina in many years, 873 SCFM Dryer Required;= (Required Capacity) /(Pressure • Enhanced formula Correction)/(Temperature • Improves adsorption Correction): (1, 1000 18 / .74 • Lower pressure drop 1145 SUM • Higher mush strength • Reduced channeling • Less dusting • Direct replacement • More efficient • Longer life 0.56 I 0.56 0.65 0.56 0.65 l 0.65 0.74 0.74 0.83 0.74 : 0.82 j 0.83 0.91 0.9 g :1.0,0.99 0.91 1.0 1.07 ! 1,10$ 1.09 1.16 f.i$ 1.27 i 1.24 1.37 ( 1.271.33 1 137 1.43 1.41 NA 1.43 NA NA f 1.58 li NA NA NA NA i 1.75 NA ? NA 1.84 r NA NA I 1.92 i - NA 1.0 1.0 1`.0 1.0 1.0 to 1.0 1.0 0.85 1.0 0.73 0.85 0.74 0.66 0.64 0.74 0.59 0.55 0.52 0.55 C: DATA SHEET — DIFFUSION SYSTEM PROJECT NAME: Oshkosh Water Filtration Plant Oshkosh, W/ 1. Data Sheet Diffusion System Type of Ozone Dissolution Fine -bubble Diffusion System Number of Contactor Basins o (2) Contactor Basins Description o (2) sets of Diffuser manifolds per contact tc mber. e diffuser manifolds to be located in cell 1 and cell 3 of each contact chamber Quantity (per Diffusion Cell) anifold Loops 4 FNo.offfusers per Manifold 8 No. of Blow -off Diffusers per manifold 4 per loop Data Sheets for Diffusers Manufacturer Assembly SUEZ Ceramic Element Refractron Model No. Z1372-H03 (7" Diffuser) Z1372-H04 (7" Blow -Off Diffuser) o� �a Materials of Construction Aluminum Oxide Diffuser w� O W 316L SS Hardware �aa � o y; ro Expanded PTFE Gaskets (Gore -Tex): aoyE N C�i NQ �a Diffuser Dome Gasket 2z Diffuser Bolt Gasket ON H Manifold Piping Flange Gaskets N Z Q Process Connections 3/" NPT 2. Diffuser Layout (see attached drawing) Diffusion S stem Data Sheet I of 2 APPROVED: DWG No, VEOLIq Water Technologies REV: VJEOLIA LEONIA',oNJT 07605 Road A 14XXX-07-0201 — PROJECT NAME: DATA SHEET — DIFFUSION SYSTEM Oshkosh Water Filtration Plant Oshkosh, WI 3. Calculations to Demonstrate Gas Distribution at the following (See calculation sheets operating conditions) : Condition 1, normal max. 1200 ppd, 10%, 1 contactor, 2 cells production 1200 ppd, 10%, 2 contactor, 2 cells Condition 2, normal max. production 1200 ppd, 10%, 2 contactors, 1 cell in each Condition 3, normal max. 600 ppd, 10%, 2 contactors, 1 cell in each Condition 4, average production production � 600 ppd, 10%, 2 contactors, 2 cells in each Condition 5, average p 1 cell 100 ppd, 10%, 1 contactors, Condition 6, min. production Condition 7, min. production 100 ppd, 10%, 1 contactors, 2 cells Gaseous Ozone/Dissolved Ozone Medium: Operating Data up to 10% by wt ozone Design: Suitable up to 14% by wt ozone 0.2 to 1.8 scfm (normal Diffuser Flow Range: a operating conditions) oMax. Diffuser Flow: 2.0 scfm ea. Bubble Diameter: 2 to 3 mm ma Efficiency: 90% (Min) 0 Contactor Cell Transfer U G w N Q Curve dwg A N see attached Headloss .C.b «� �QoZ w a � 4. Headloss Calculation � 14 in. WC N N Headloss at min, flow flow 22 in. W Headloss at max. N c O 2of2 TITLE: stem Data Sheet ;NECKED: Diffusion S •7 DWG No. VEOLIA Water 7echnologles -e Road A 4XXX-07 020 1 APPROVED: LEONI�A �NJ7 r0760 i V . OLIA ` \'\ ) _\ ` a( ) k£2 \ z, \ k \ \\\ \ / \ 9 $ �\ I � /�\ I \ \ \ 0 I 0 r J Q w W F-- g V R�e-! �' o y 3 F 2 u N N D (o o� C Subject: Oshkosh OK Jacobs Contactors Ozone Requirement (Total) Ozone Requirement (Contactor) Ozone Concentration Total Gas Flow Gas Flow per Contactor Gas Flow Split per Cell Gas Flow to Cell 1 Gas Flow to Cell 2 No. of Diffusers per Cell 1 No. of Diffusers per Cell 2 Gas Flow Split per Cell Gas Flow to Cell 1 Gas Flow to Cell 2 No. of Diffusers per Cell 1 No. of Diffusers per Cell 2 (designed for 50/50 split) 1200(10)1 cont, 2 cells 1200 Ibs/day 1200 Ibs/day 10 % by weight 100.E SCFM 100.6 SCFM % Flow 100 100,E SCFM 0 0.0 SCFM 32 3.14 scfm/diff N.G. 0 4DIV/01 scfm/diff 0 4DIV/0! scfm/diff % Flow 50 50.3 SCFM 50 50.3 SCFM 32 1.57 scfm/diff V 32 1.57 scfm/diff V 10/7/2023 - 10:10 AM Contactor Calc Oshkosh, WI 32 Diff 1200(10), 60 (4) Rev. 1 9-24-23.xis 12000 0) 2 cont, 1, 2 cells Subject: Oshkosh OK Jacobs Contactors 1200 Ibs/day Ozone Requirement (Total) 600 Ibs/day Ozone Requirement (Contactor) 10 % by weight Ozone Concentration 100.E SCFM Total Gas Flow 50.3 SCFM FIOW Gas Flow Split per Cell 50 25.1 SCFM Gas Flow to Cell 1 50 25.1 SCFM Gas Flow to Cell 2 32 0.79 scfm/dill � No. of Diffusers per Cell 1 No. of Diffusers per Cell 2 (designed for 50/50 split) 32 0.79 scfm/dill v 10/7/2023 -10:25 AM Contactor Calc Oshkosh, WI-32 Diff_120000), 60 (4) Rev. 1 9-24-23.xls Subject: Oshkosh OK Jacobs Contactors Ozone Requirement (Total) Ozone Requirement (Contactor) Ozone Concentration Total Gas Flow Gas Flow per Contactor Gas Flow Split per Cell Gas Flow to Cell 1 Gas Flow to Cell 2 No. of Diffusers per Cell 1 No. of Diffusers per Cell 2 1200(10) 2 cont, 1, 2 cells 1200 Ibs/day 600 Ibs/day 10 % by weight 100.6 SCFM 50.3 SCFM % Flow 100 50.3 SCFM 0 0.0 SCFM 32 1.57 scfm/diff V n wnn /,-, 10/7/2023. 10:23 AM Contactor Calc Oshkosh, WI_32 Diff 1200(10), 60 (4) Rev. 1 9-24-23.xis Subject: Oshkosh OK Jacobs Contactors Ozone Requirement (Total) Ozone Requirement (Contactor) Ozone Concentration Total Gas Flow Gas Flow per Contactor Gas Flow Split per Cell Gas Flow to Cell 1 Gas Flow to Cell 2 No. of Diffusers per Cell 1 600 (10) 2 cont, 2,1 cells 600 Ibslday 300 Ibslday 10 % by weight 50.3 SCFM 25.1 SCFM Flow 100 25.1 SCFM 0 0.0 SCFM 32 0.79 scfm/diff p #DIV/O! scfmldiff Kin of Diffusers per Cell 2 0 #DIV/01 scfmldiff V Cont actor Calc Oshkosh, W_32 Diff_1200(10), 60 (4) Rev. 1 9-24-23•xls 10/712023 -11:32 AM Subject: Oshkosh OK Jacobs Contactors Ozone Requirement (Total) Ozone Requirement (Contactor) Ozone Concentration Total Gas Flow Gas Flow per Contactor 600 (10) 2 cont, 2,1 cells 600 Ibs/day 300 Ibs/day 10 % by weight 50.3 SCFM 9r .1 -.. "I'-lowto Cell 50 12.6 SCFM No. of Diffusers per Cell 1 50 12.6 SCFM No. of Diffusers per Cell 2 (designed for 50/50 split) 32 0.39 scfm/diff V 32 0.39 scfm/diff V 10/7/2023 _ 11:35 AM Contactor Calc Oshkosh, WI 32 Diff 1200(10), 60 (4) Rev. 1_9_24.2 3.xls Subject: Oshkosh OK Jacobs Contactors Ozone Requirement (Total) Ozone Requirement (Contactor) Ozone Concentration Total Gas Flow Gas Flow per Contactor Gas Flow Split per Cell Gas Flow to Cell 1 Gas Flow to Cell 2 No. of Diffusers per Cell 1 100(10) 1 cont, 211 cells 100 Ibs/day 100 Ibs/day 10 % by weight 8.4 SCFM 8.4 SCFM Flow 100 8.4 SCFM 0 0.0 SCFM 32 0.26 scfm/diff 0 #DIVl01 scfm/diff V 10/712023 -11:14 AM Co ntactor Calc_Oshkosh, WI_32 Diff 120000), 60 (4) Rev. 1 9-24-23.xls Subject: Oshkosh OK Jacobs Contactors Ozone Requirement (Total) Ozone Requirement (Contactor) Ozone Concentration Total Gas Flow Gas Flow per Contactor 10000) 1 cont, 2,1 cells 100 Ibs/day 100 Ibs/day 10 % by weight 8.4 SCFM A A Qnre. uas f low to Cell 1 % Flow Gas Flow to Cell 2 50 4.2 SCFM No. of Diffusers per Cell 1 50 4.2 SCFM No. of Diffusers per Cell 2 (designed for 50/50 split) 32 0.13 scfm/diff N.G. 32 0.13 scfm/dill N.G. 10/7/2023 _ 11:13 AM Contactor Calc Oshkosh, WI 32 Diff 1200(10), 60 (4) Rev. 1_9-24-23 xls CV r O Q ,Itr N 1: = w x Cl? CV N (V IN m N N 600 O v O � O (NWn-i" "3- VM d0 S3HONO SSOldy3H C; 00 r 0 1 0 1 6 0 Q Ir )H -0 zone Ir r Treatment ,ons - - _ a rooa addition, any function that can be set or monitored 25 �o w/W ne, In processing, and research applications. The 465H has from the front panel can be remotely set or viewed been designed to give accurate and stable readin s CS over long time periods with lift, 9 through the bi-air, e or no maintenance arning alarms or calibration. The Model 465H is available in a NEMA 4X wall mount enclosure. times drift The sensor module contained in the Model 465H uses detectors which havea Wa spectral sensitivi n very narrow band of e auto -zero function h% eliminating the need f a Phi �- . 1 wl rcenrration alarms ® Temperature and pressure compensation (standard) s Optional Ethernet band pass filters which are subject to deter' ior UV oration by UV a Sect or humidity. Two detectors are used: one for the ozone measurement, and the other to compen- sate for changes in UV lamp intensity. This unique a Othi design provides a sensor which will operate for ex- tended periods without calibration or maintenance. Built-in diagnostics provide warning signals in case operating parameters are out of range.: Test values can be viewed while the Model 465H is operating, Law) Princi le UV Absorption (Beer Lambert —.. — ® Measurement — - . _.......... - -- - ..._..__.._._.._. - _...__-- 0-5% w/tv to 0-25% w/w m Ranges 3 0-100g/Nm to 0-4009/Nm3 -- ----- ----- -- _._ ......._.._.._....._....._.._ % w/w, g/Nm3 --- _....._......_.— + 1% of Full Scale ...... __-._.......—.___.-- . aAccuracy ....____.._.__ ® Precision/Repeatability _.._._._.._._..__.—....__._._ ± 0.5% of Full Scale ® Display Resolution 3 0.01 % w/w, 0.1 g/Nm <30 seconds to 95% ® Response Time Pressure, Temperature • Compensation (NTP = 273.15K, 760mmHg) s Gas Inlet Pressure Range 3.0 - 30.0 psig _ 0.2 - 2.0 LPM ® Gas Flow Rate a Temperature Range 5-45°C — x 15.60" x 6.90' a Dimensions (H x W x D) NEMA 4X-16.85' (428 mm x 396 mm x 175 mm) NEMA 4X -15.0 Ibs (6.8 kg) Weight - ----- --- 110-240V, 50/60Hz, 74W a Power 0-5V or 4-20mA isolated output Analog Output OK, Invalid Reading, ® Status Outputs System UV Lamp Fault, Pneumatic Error (optional RS-485) 57.6 Kbaud, DB-9 connector ® RS-232 (Op s Approvals CE e Degree of Protection IP65 (NEMA 4X) (NEMA) � Warranty 1 year 465M 465H 454 452 430 Wt + 465L 470 Printed documents are uncontrolled SAL0000?OE (DCN 8148) 07.0E 19 Specifications subject to change without notice All specifications are based on constant conditions 049Tj� 9970 Carroll Canyon Road, San Diego, CA 92131 •USA � �� ���� rel.858-857-9800 • api-salesQteledyne,com DNV-GI (yvV e> yOulool�.. vuwv+�. teledyne-api-COM v _V T_, .Ma nq isosoot I) Ethernet The Model 465M is a microprocessor based Built-in diagnostics provide warning signals in medium range ozone monitor for measuring case operating parameters are out of range. process ozone concentrations in water Test values can be viewed while the Model ch 465M is operating. These displays, warnings, treatment, food processing, and resear' applications. The design has been specifically and self -diagnostics, along with the modular optimized for applications requiring the design, allow maximum uptime. In addition, +; that can be or monitored from measurement of ozone at near -ambient tineef pressure such as water treatment contactor thf off -gas measurement. The Model 465M has been designed to give accurate and stable readings over long time periods with little or no maintenance or calibration. The Model 465M is for available in a NEMA 4X wall mount enclosure. o iments The sensor module contained in the Model i alarms 465M uses detectors which have a very narrow the need 1,,nri of spectral sensitivity, eliminating compensation for UV band pass filters which are subject to deterioration by UV or humidity. Two detectors a are used: one for the ozone measurement, and the other to compensate for changes in UV lamp intensity. TELEDYNE AN ulo©k{ Everywhereyo specifications • Measurement Principle UV Absorption (Beer Lambert Law) • Ranges 0-1,000 ppm to 0-10,000 ppm 0-5g/Nm3 to 0-50 g/Nm3 0-1% w/w to 0-3% w/w • Measurement Units ! % w/w, g/Nm3 ppm • Accuracy ± 1% of Full Scale • Precision/Repeatability 5% of Full Scale ± 0�,4 ® Display Resolution .001 % w/w, 0.01 g/Nm3 • Response Time onds to 95% • Compensation Pressure, Pressure, Temperature = 273.15K, 760mmHg) • Gas Inlet Pressure Range 11.0 —16.0 psia • Gas Flow Rate ..... _..........__............._ 0.8 LPM _ • Temperature Range 5-45°C • Dimensions (H x W x D NEMA 4X—16.85" x 15.60" x r; qn^ NEMA 4X —17.2 Ibs (7.8 kq) Specifications subject to change wthout notice. All specifications are based on constant condition • Power • Analog Output • Status Outputs • RS-232 (Optional RS-485) • Approvals • Degree of Protection (NEMA) • Warranty 110-240V, 50/60Hz, 74W 0-5V or 4-20mA isolated output System OK, Invalid Reading, UV Lamp Fault, Pneumatic Error 57.6 Kbaud, DB-9 connector CE IP65 (NEMA 4X) 1 year s. Printed documents are uncontrolled. SAL000022E (DCN 8148) 07.02.19 The Model 465L UV Photometric Ozone Monitor is an extrernely stable analyzer, ideal for critical low-level ppm safety and process applications I 3 ppr� is calibration is NIST traceable and the included r and High -High pressure and temperature compensation ensure high accuracy under all conditions. larms The Model 465L is available in a 19" rack mour- or NEMA 4X wall mount enclosure and can be Purchased either as a single stream unit or as a multi -channel unit capable of monitoring up ions available f to six individual sample streams. 465E The Model satety monitoring ; or has beendesigned to deliver excellent ?rogrammable concentration alarms performance, high reliability and simple operation. Operating parameters can be easily emperature and pressure compensation set up in the field using the operator-frie standard) menu driven software, ndly Iptional Ethernet Built-in diagnostics provide warning signals in case operating parameters are out of range. Test values can be viewed while the Model no Ozone, hanner MORONS ® Measurement Principle UV Absorption (Beer -Lambert Law) • Measurement Range — - - --- - - --- m to 0-500 ppm From 0-1 pp _--_-__.._..__-_-_____ pprnv, pbv, pphm, Pg/m3, mg/m' pp p • Units • Precision // Repeatabilitynrecisio --- ±0.5% of full state • Dis la Resolution p---.._...__. _001 ppm _.______. --- -._— scale • Accuracy �— _ 005 ppm/month, non -cumulative • Zero Drift (.050 ppm/month Ranges >20 ppm) • Lower Detectable Limit (LDL) .003 ppm - —_----- ------ _----- -- ----------- ------- < 30 seconds to 95°° • Response Time -_— Latching/non-latching, operator • Relay Mode selectable • Stream Selector C cte Time 1 min. to 6 min., operator selectable • Sample Flow Rate 0.8 liters/minute rature SIC - 45`C • Operating Tempe Range • Dimensions (HxWxD) Rack M 522" (133 mm) x 19' (483 rnm) x 15.3" (388 mm) NEMA 4X-16.85" (428 mm) x 15.60" (396 mm) x 6.90' (175 mm) Rack Mount -12.6 Ibs (5.73 kg) • Weight NEMA 4X -15.1 Ibs (6,85 kg) 100 - 240VAC, 50/60 Hz, 74W .._... • Power _..-- ------ _......_....---...._..._...--._..._.._..._..._.__..__._..._..._... 0-5V or 4-20mA isolated output ---"-- • Analog Output _ F(S rm C mC/5A • High Current Relay Outputs It, Ala ystem OK,Global HI -HI Alarm) • Low Current Relay Outputs Dry Contact Load (Channel D?HI mA (3 or 6 channel, 3 per channel) Resistive Alarm, HI -HI Alarm) ......... System OK, Invalid Reading, • Status Outputs Pneumatic Fault, UV Lamp Fault • Stream ID Outputs Channel 1 through 6 • RS-232 (Optional RS-485) 57.6 Kbaud, DB-9 connector - ........_..__..__.. _....... __. • Approvals _...CE_.....__.._.. IP65 (NEMA 4X) • Degree of Protection (NEMA) • Warranty _ 1 year Soecifications subject to change without notice. All specifications are based on constant conditions. .arroil Canyon Road, San Dieg 3-657-9800 ® api-6ales@tek v.teledyne-api.ca eledvne API Printed documents are uncontrolled. SAL000021D (DCN 8114) 04 26.19 S Series Specification Sheet Accurate real-time • ir quality affordable Designed for those who need a handheld device to gather real-time information on the surrounding air. A simple tool for professionals and enthusiasts alike, the portable monitors can be configured with 28 different gas and particle sensors. Suitable for measuring target gases in ambient air at different concentrations in outdoor or indoor environments. What are they for? Environmental impact assessments Indoor air quality testing Checking air pollution "hot spots" Educational tool for schools community air pollution monitoring Validating air quality models Health and safety compliance Personal exposure monitoring What are they for? Interchangeable sensor heads enable measurement from a choice of 16 different gases or particulates. pM ,a PM, voc' 03 NO, CO co ' z so, cHp H,s NH3 Glz CH, Hz NMHC CzGI TRH': G SO Who is it for? Air quality professionals who need real-time defensible measurements community groups who need cost-effective scientifically credibleair quality data Educators who want students to learn about air pollution in a way that supports STEM Health and safety managers who need to demonstrate safe environments • Researchers who want to collect scientifically robust data on a limited budget Environmental consultants who needa portable device for periodic and discrete monitoring Citizens who want to measure their personal exposure to air pollution ... � , ani'y F• salb3(NBb!?�: itc�.C:., �. ��. 6�.. `t,bi,�, _..� Specifications I S Series portable air quality monitors S Series system specifications Measurement units Gas: ppm or mgJm31 Humidity: Series Series 300 500 %I Temperature °C or °F Reading functions Instant, minimum, maximum, ✓ ✓ average Sensor head Active fan sampling to ensure high accuracy measurements, ✓ ✓ Sensor head calibration interchangeable, replaceable ✓ ✓ Zero and span calibration Temperature & humidity sensor Range -40°C to 124°C (-40°F to 255°F); ✓ ✓ Range 0 to 100"%RH Environmental operating conditions Temperature: -5°C to 45°C I Humidity: 0 to 95% non ✓ ✓ Display status indicators -condensing ✓ ✓ Battery, sensor, standby Power supply 12Vdc (Power adaptor/charger supplied100-250Vac) ✓ ✓ Rechargeable batter Y Lithium -ion 12Vdc 2700 mA.h ✓ ✓ Enclosure material and ratio 9 PC and ABS; IP20 and NEMA ✓ ✓ 1 equivalent Size (L x W x D)195 x 122 x 54 (mm); 7% x 4Y x 2% (in) (with sensor head) ✓ ✓ Weight <460g; <16oz (with sensor head and battery) ✓ ✓ Approvals Part 15 of FCC Rules; EN 50082-1: 1997, EN 50081-1: 1992 ✓ ✓ Analog output 0-5V ✓ ✓ Clock function Real time ✓ ✓ Digital interface RS-232 to USB ✓ Data logging Up to 8,188 records (2706 incl. Temp/RH) ✓ PC data logging (Windows) Software and data cable supplied. Link ✓ data to a specific location and monitor For the full range of available sensors heads, visit our website; www aPr_ oa_ a com or download the list. Optional Accessories } ,fi lgjppp- Temperature/ RH Wall Bracket Sensor Industrial Enclosure Remote Sensor Kit IP41 Remote Sensor HH TRH AS R33 HH ENC AS R10 Kit AS R13 Ac� 3 ti Cigarette Lighter Lithium Battery Carry Case Small Adaptor AS R36 Carry Case Large AS R32 AS R40 AS R41 T: �64 �4 623 `3013 E: FC C E C =ales��;,ere,�„ �ai.corr+ W: tie: TELEDYNE ANALYTIC MODEL 335® 4� 0fdg?&l lft)vvY-fl Personnel safety is a primary issue in nearly every industry, and no factor is of greater importance than assuring an appropriate level of oxygen in an enclosed area. Teledyne's Model 3350 Control Room Oxygen Monitor accurately measures the concentration of oxygen in control rooms, closed atmospheres, critical breathing circuits, and other applications that require the fail-safe monitoring of breathable, ambient air, Simple to use and maintain, this unit shoulders the burden of personnel safety with the quality and reliability offered by the Teledyne name. The 3350 is a microprocessor -based oxygen alarm monitor for real-time measurement of the oxygen content of the atmosphere surrounding its sensor. The standard instrument is configured to run from an AC power source and is also available with an optional, continuously charging, DC battery backup. The rated battery life is approximately 17 hours configured in failsafe mode and 48 hours in non-failsafe mode. DUAL OXYGEN ALARMS The alarm setpoints provide an operational band that covers all acceptable oxygen concentrations. If the oxygen level at the sensor crosses the adjusted setpoint of one of the alarms, that alarm will cause the switching of relay contacts. Designed in consideration of OSHA specifications, the standard factory setting of the two alarms provides a CAUTION alarm at 20% oxygen and a DANGER alarm at 19.5% oxygen. To cover special situations, a limited amount of adjustment is possible. Both alarm setpoints are factory set (internal) to prevent tampering or resetting by unauthorized personnel. When an insufficient oxygen concentration triggers either alarm, a red panel light and an audible annunciator are energized. The alarms remain energized until the oxygen concentration has been elevated above the trigger point. BATTERY BACKED STANDBY POWER An optional Battery Backed Standby Power Configuration is offered for potential power failure or "brown out" conditions. With this feature, power outages will not interfere with a properly working alarm. The standby power source uses a rechargeable lead acid battery. If the AC power is interrupted, the stand-by power supply automatically supports analyzer operation. Periodic testing of the battery pack is possible through a simple pushbutton inside the instrument's control panel. MAINTENANCE -FREE SENSOR The 3350 uses a patented Micro -fuel Cell to measure the concentration of oxygen in breathable air. This sensor is a sealed electrochemical transducer with no electrolyte to change or electrodes to clean, so it is virtually maintenance free. When it reaches the end of its useful life, it is easily replaced. SIMPLE CALIBRATION Periodic calibration is quickly and easily accomplished with no specialty gas requirements. The Micro -fuel Cell produces a linear output from zero to 100% oxygen so ambient air or readily available instrument grade air (20.9% oxygen) can be economically used for calibration. Also, since the Micro -fuel Cell has an absolute zero, no zero gases are needed. EASY TO INSTALL The 3350 is designed for easy installation. Mount the unit to a wall or bulkhead, connect AC power, and the installation is complete. The unit is lightweight with a slim profile, eliminating the need for special reinforcement in most installations. (Note: Teledyne recommends consulting a safety expert to select a suitable location for installation.) REMOTE PROBE AVAILABLE A special version of the 3350 is available with a remote -mountable oxygen probe. This option permits the user to install the oxygen probe inside the control room, while the control unit is mounted outside. This allows personnel to see the analyzer and confirm a safe level of ambient oxygen is present before entering the control room. Built for reliability and Performance SPECIFICATIONS FEATURES Range: 0-25% oxygen • Large, bright, LED meter readout Sensitivity: 0.5% of full scale • Nylon cell holder Accuracy: ±2% of full scale at constant temperature; full scale (over operating temperature range, • Audible and visual alarm indicators ±5%O of once the system has reached equilibrium at a • Simple pushbutton controls • Long -life, maintenance -free Micro -fuel Cell oxygen sensor con than 20 seconds at 25°Cstant temperature) • Unaffected by oxidizing gases Response time: temp: 90° in less 32 to 122°F (0 to 50°C) • Fast response and recovery time Operating & storage 0-95%von-condensing • Microprocessor based electronics spanning at 20.9% oxygen Relative humidity: altitude: 6562 feet (2000 meters) • Air calibration range for convenient alarms, Form C relay contacts, configured Maximum Reproducibility: ±1% of full scale • Two factory preset as failsafe or non-failsafe Sensor type: B-3 class Micro -fuel Cell • Two analog outputs: two for measurement (0-10 Vdc and Display: LED non-failsafe 17 hours negative ground 4-20 MA) 48 hours (non -alarm conditions) and rugged, wall mounted NEMA-4 rated enclosure Battery life: (non- alarm conditions) failsafe • Compact • CE Mark approval Power requirements: AC 100 to 240 Vac @ 50/60 Hz, 0.3A Max; battery maintains a 12 VDC lead backup version charges and OPTIONS OP acid battery (10mA Max) • Battery back-up Signal output: Voltage: 0-10 VDC, negative ground 4-20 mA, negative ground (15V max open • Power requirement: Current: operating circuit)10 VDC / 500 ohms maximum op 9 range 100 / 220VAC, Audible alarm: 12-15 VDC, 4.3 mA max 50 / 60 Hz _ Enclosure: wall mounting, NEMA-4 enclosure • Special ranges ,• Dimensions: 8" wide x 101, high x 6" deep x 25.4 x 15.2 cm) • Special remote p (20.3 probe o Alarms: • Provisions o Factory set: Caution 20.0% for conduit- Danger -19.5% in power 0SSEMBPROBE connection ASSEMBLY �, Sensor failure: Audible - buzzer Visual - red indicator lamps ,•,•,,,,,n,.E CLIOVAIYTG.HOLE0 ZOO IM81 +----� POWER 10B0, CABLE GLAND %1 TELEDYNE ANALYTICAL INSTRUMENTS A Teledyne Technologies company 16830 Chestnut Street City of Industry, California 91748, USA TEL: 626-934-1500 or 888-789-8168 FAX: 626-934-1651 EMAIL: ask tai@teledyne.com www.teledyne-ai.com Warranty Instrument is warranted for 1 year against defects in material or workmanship NOTE: specifications and features will vary with application. The above are very established NOTE: All validated specifications during design, , but srare subject o change without n0tiGet to be construed as test criteria for every p uct ERTp r �==W @ 2006 Teledyne Analytical Instruments, A Teledyne Technologies ompany. All rights reserved. Printed in the USA. 09106 Cermet 11 Hygrometer t erature, or gaseous moisture The hygrometer of choice for the measurement of dew point, emp applications wi th a choice of units of measurement or where pressure compensation is required. michell.com MICHELL www. ®nstru ents mHELLments www.michell.come Technology: impedance TheCmmet uses impedance technology, advanced ceramic sanxo: The operation onthe dielectric property o[water mmec active porous insulating layer sandwichei conductive material deposited on a cerat Water has a very high dielectric compari the active layer and the background be detected easily. The active layer is very thin — lesp'th6n porous top conductor that allows'ik6ter into the active layer is less tha�`OA mic the sensor to respond very rapidly to ct surrounding it both when mbiftore, deci increases in the sensor envir nmenL �� _.~~.~^~.~~..°~..."..~~"~^._~~~~..~........°~~~..~..~.~...~....~.~~...~~~."~..°.~~.^..^~ mnmww���J���U.�0mM OMICHELL instruments Technical Specifications Sensor Measurement Range d00 to +20°C (-148 to +68°F) dew ` Options Accuracy (dew point) point fi°C from -60 to +20°C dew point Qutputs (t1.8°F, -76 to +68°F dew point) f2°C from -100 to -60°C dew point (t3.6°F, -148 to -76°F dew Enclosure point) Stainless steel Ingress Protection NEMA 4 in protection and accordance with Alarm Relays standard NEMA 250-2003 and IP66 in accordance with standard BS EN 60529:1992 Storage Temperature -40 to +109°C (-40 to +165°F) Cable Operating Pressure From vacuum to 40 MPa 000 66rg/5801 psig) (max) Flow Rate 1 to 5 I/min (2.1 to 10.5 scfh) Gas Velocity 0 to 10m/sec (0 to 32.8 ft/sec) Process Connection Sensor 5/8"UNF parallel thread Dimensions Calibration Traceable to NIST and UKAS Analyzer Resolution 0.1 °C from -80 to +20°C dew point (0.18°F, -112 to +68°F dew point) 1°C from -100 to -80°C dew point (1.8°F, -148 to -1120F dew point) Alarm Relays Two user adjustable isolated 10A form'C' rated at 240 V AC or 24 V DC Power supply Universal 85 to 265 V AC, 50/60 Hz or 95 to 370 V DC Operating Conditions operating Temperature Analyzer: 0 to +50°C (32 to +122°F) Sensor: -20 to +50°C (-5 to +122°F) 1 or 2 additional 5 A relays (max 4 total) n/o type fully user configurable and adjustable over the full range, full choice of units and sensor fault alarm functions Standard 2 m (6.56 ft) (1200 m/3937 ft max) SENSOR 45.0mm (1.77') 46 0—, 27A 027.0. O39" 025.4mm 3; 5/5° UNF (toot' z.amm OOT .55 0mm 2 16' ® 0 030.� �' �'} _ . J' BONDED SEAL 5/8" UNF SENSOR BLOCK MONITOR t 96 mm (3.78110 qG 1 tea❑ oru®o NPT 9292 nim (3.62 in) e 6 a� E F E�o PA14EL CUTO Ur Michell Instruments Ltd, Rotronic Instruments Corp, 135 Engineers Road, Suite 150, Hauppauge NY 11788 Tel: 631 427 3898, Email: us.info@michell.com, Web: www,michelf.com/us Michell Instruments adopts a continuous development programme which sometimes necessitates soecifi—ti Issue no: Cermet II_97169_V2.1_US_0518 MICHELL � E . ...... � . . _ . �. © 2018 Michell Instruments Instruments Flow Meter Sed i e S 5 T r 4 F The Kurz 534FTB is designed with built-in inlet and outlet piping reducers/ expanders to produce exceptional immunity to upstream and downstream flow disturbances caused by elbows, valves, and line size changes. The patented technology results in output with exceptional low end -to -en pressure drop and the fastest response to velocity and temperature changes in the industry. The Kurz 534FTB in -line now meter includes the qualities and features found in all Kurz constant temperature thermal flow meters that make them outperform all other currently available thermal mass flow meters, including: g The highest repeatability, accuracy, and reliability available The fastest response to temperature and velocity changes in the industry Constant temperature thermal technology High turndown ratio Low flow noise Continuous self -monitoring electronics that verify the integrity of sensor wiring and measurements Sensors do not overheat at zero flow using a unique constant temperature control method and Power limiting design Sensor lead length independent circuitry Sensor lead length independent circuitry Zero velocity as a valid data point Completely field configurable using the local user interface or via a computer connection ° Supports HART, Profibus DP, and Modbus communication Protocols Velocity-terperature mapping for wide ranging velocity and temperature User -defined binary gas compositions or up to five multiple gas calibrations Flexibility with transmitter - attached or transmitter -separate designs Patented digital sensor control circuit (US 7,418,878) on,uG�ect r� chonaa t;tithnut r..!ice Cerfu Yor yr/t !:urz un;7re trn complete sr�dficatiors vnd:,,,��.;.... INSTRUMENTS INC. Kurz Instruments is dedicated to manufacturing and marketing the best thermal mass flow meters available and to support our customers in their efforts to improve their businesses. Applications Process & specialty gases Compressed air Fuel flow Natural gas metering Solvent & VOC recovery NOx control using ammonia Flow calibration Air sampling SPECIFICATIONS o Mass flow range Up to 7,016 SCFM (10,944 NCMH) depending on model and calibration option Flow accuracy (SCFM at laboratory conditions) ± (1 + 2000 x A/F)% where F=SCFM, A=flow body area (ft2) 0.25% reading repeatability Velocity time constant 1 second for velocity changes at 6,000 SFPM (constant temp) ® Process temperature time constant 8 seconds for temperature changes at 6,000 SFPM (constant velocity) ® Temperature accuracy ± (0.5% of reading +1°C) for velocities above 100 SFPM ® Electronics operating temperature Integral display -13°F to 149°F (-2S°C to 65°C) Remote aluminum display -40°F to 149OF (-40°C to 65°C) Remote polycarbonate display -13°F to 122°F (-2S°C to 50°C) PROCESS CONDITIONS Process pressure rating Up to 300 PSIG (20 BARg) a Process temperature rating -40°F to 257°F (-40°C to 125°C) APPROVALS a EPA mandatory GHG certification 40 CFR 98.34(c)(1) TRANSMITTER FEATURES a Aluminum (Type 4, IP66) dual chamber polyester powder -coated enclosure Adjustable display/keypad orientation ® Two optically -isolated 4-20 mA outputs 12-bit resolution and accuracy Maximum loop resistance is 5000 at 18 V DC, 8000 at 24 V DC, 14000 at 36 V DC SUPPORT & ELEMENT COMPONENTS 0 Sensor material C-276 alloy all -welded sensor construction ® Input power AC (85-264V 50/60 Hz, 24 watts max.) or DC (24 V ±10%), 1 A max. ® Solid state relays Optically isolated, 0.5 A, 24V AC/DC maximum Integral or remote user interface Easy -to -use interface Backlit display / keypad 2-lines of 16-characters each User -configurable flow display (scrolling or static) • User -configurable English or metric _ units for mass flow rate, mass velocity, and process temperature ,,C, °F, KGH, I<GM, NCMH, NLPM, NMPS, PPD, PPH, PPM, SCFH, SCFM, SCMH, SLPM Two optically isolated solid-state relays / alarms Configurable as alarm outputs or pulsed totalizer output, or air purge cleaning a Built-in flow totalizers and elapsed time o Alarm output conformity NAMUR NE43 European Union CE compliance EMC, LVD, PED, ROHS, and WEEE CSA, ATEX & IECEx approvals for Nonincendive, Flameproof, and Explosion -proof EN IEC 60079-0, EN IEC 60079-1 EN IEC 60079-15, CSA Class I, Div.1 and 2 ® IEC 61508, SI1-1 via TUV Rheinland a User -configurable digital filtering from 0 to 600 seconds ® Configuration/data access USB or RS-485 Modbus (ASCII or RTU) Meter memory 200 recent events, top 20 min/max, and 56 hours (10 second samples of trends) a 3-year warranty 0 Sensor support 316L stainless steel a Sensor flow body diameter options Available from 1 /2" to 8" a Connection type Raised -face flange (Class 150 ANSI 1316 Or Class 300 ANSI B16.5) or male NPT pipe ends 0 3-year warranty OPTIONS Enclosures Aluminum or remote -only stainless steel or polycarbonate Multiple gas calibrations with up to five curves loaded in memory ® User -defined binary gas composition ® Communication protocols HART (v7 FSK) and PROFIBUS DP Is One 4-20mA non -isolated analog input a Digital input dedicated to zero -mid -span drift check ® Pulsed output as a remote flow totalizer i Hardware accessories Available hardware includes sun shades, ball valves, cable glands, conduit seals, and cable NA fflk n C E Gx c } �/, SP�S COMMUNICATION PROTOCOL PROCESS TEMPERATURE & COMPENSATION Temperature influences the physical pro---------------- perties of gases, so temperature compensation is required for a thermal sensor to accurately measure gas flow rates. ® Standard Temperature Compensation (STC) is used for process temperatures from 0°C to 125°C over a moderate velocity range. ® Velocity Temperature Mapping (VTM) is used when the process temperature and gas velocity vary widely. Multiple velocity calibrations are stored in the meter. VTM compensation is based on air; specific gas correlations are required to ensure accuracy at high terperatures. The flow area (Fa) is the flow measurement section of the 534FTB, as shown in Parent Number table. SPECIALTY GAS VELOCITY CALIBRATION There are two types of gas calibration: • Laboratory gas calibrations are performed with gases of high purity and are NIST traceable. Values above the calibrating facility limit are correlated up to the specified range. Customers must specify the calibration process pressure. • Correlation gas calibrations are based on experimental data correlated to an Air calibration at ambient pressure and temperature. The flow element is calibrated in Air, and then an additional calibration data sheet is generated using the correlation factors. All correlation calibrations include velocity -temperature mapping. Add ±5% of reading to the accuracy specification when using a correlation calibration. -or Oxygen gas, the customer is responsible for ensuring the mass flow ;ensor is clean of hydrocarbons and safe for Oxygen use. d$1-646-59111www.Kurzlnstruments.com ANALOG & DIGITAL INPUTS All options include USB interface with ASCII text and Modbus protocol through RS-485. The 4-20mA analog outputs (AO) are used for flow rate and/or temperature, or one AO for PID now control. All AO are NAMUR NE-43 compliant. Relay digital outputs (DO) can be alarms, EPA zero -mid -span drift is active, or pulsed totalizer function. PID uses one 4-20MA output for the flow controller. The EPA zero -mid -span drift check requires a contact closure to start the drift check. All 4-20mA outputs are used during the Drift Check Calibration process. EPA zero -mid -span drift check can be initiated using digital inputs (DI), elapsed runtime automatic drift check, Modbus, or HART. The 4-20mA analog input (Al) supports feedback to the device. ire Thermal Mass Flow Meter 2411 Garden Road . Monter�CA3940800-424-7356. 831-646-5911 (www.Kurzlnstruments.com SERIES 534FTB OUTLINE DRAWINGS DIRECTLY ATTACHED ELECTRONICS ENCLOSURE (TA) SHOWN WITH MODEL 534FTB-0813 (SHOWN WITH DISPLAY IN STANDARD DISPLAY ORIENTATION) FEATURE 11 OPTIONS A& F (NOTE3) DIRECTLY ATTACHED ELECTRONICS ENCLOSURE (TA) SHOWN WITH MODEL 534FTB-32B, FEATURE 1, OPTIONS A & F (SHOWN WITH DISPLAY IN STANDARD DISPLAY ORIENTATION) (NOTE 3) FLANGES (STANDARD) MNPT(OPTIONAL) (SEE FEATURE 3) REMOTE ELECTRONICS ENCLOSURE SHOWN WITH MODEL 534FTB-32B FEATURE 1, OPTIONS D & I CONDUIT SEALS - (OPTIONAL) (TYPICAL) 3!CFNPTQYPICAL) -' YAPPROVALTAG PT PLUG N LABEL OUND LUG -32SCREW 0 6Li OW DIRECTION SEEAR I - L1 - (SEETABLE2) 3!4° FNPT (TYPICAL) POWER, GROUND,ANDOUTPUTS ANDLCONDUITBY CU TOMER INS ,`°-'` CAUTION LABEL -� GROUND LUG -� 11P32SCREW IDTAG (OPTIONAL) FLANGES (STANDARD) NINPT (OPTIONAL) (SEE FEATURE 3) FLOW z=====> 314' FNPT (TYPICAL) PONER,GROUND,AND OUTPUTS SHIELD EDCABIE,SEALS, FITTINGS. � AHp CONWRBYCUSTOMER CAUTION LABEL' GROUNDLUG #10.M SCREW IDTAG (OPTIONAL) -\) FLOW L - TABLE 2) SAFETY APPROVALTAG 31V MNPT PLUG DuAELECTRONICS ELECTRONICS ENCLOSURE FLOW DIRECTION H ARROW (SEE TABLE 2) I Li (SEE TABLE 21 L (SEE TABLE 2) SAFETY APPROVALTAG 314° MNPT PLUG DUkLCHkMBE ELECTR IN ELECTRONICS ENCLOSURE H FLON DIRECTION (SEETABLE 21 ARROW I - L1 -- (SEETABLE2) POKER, GROUND,&OUTPUTS SAFETYAPPROVALTAG SHIELDED CABLE, SEALS, RTNNGS, AND CONDUIT BY CUSTOMER 314" MNPT PLUG &CONDUCTOR SHIELDED CABLE IN DUALCCAUTION LABEL HAMBER RIGID CONDOR OR CABLE WITH BONDED SEAL BY CUSTOMER ELECTRONICS O PERIMETER ENCLOSURE VIEWING LENS GROUND LUG DISPLAY MAYBE ROTATED 190' FOR PROPER VIEWING DIRECTION Y1432 SCREW CONDUIT SEALS �' (O TIONA) (TYPICAL) (TYPICAL) SENSOR ELECTRONICS FOR REMOTELY ATTACHED ELECTRONICS ENCLOSURE (TS) W1 DISPLAYKEYPAD OPTION (SHOWN) IDTAG (OPTIONAL) FLOV - L (SEETABLE 2) LANGE$(STANDARD) ANPT(OPTIONAL) SEE FEATURE 3) FLOW BODY ASSEMBLY FOR REMOTELY ATTACHED ELECTRONICS ENCLOSURE (TS) (NOTE 1) (NOTE 3) ' _ ' ` 1-01+0-"39)11 www.Kurzlnstr'uments.com SERIES 534FTB OUTLINE DRAWINGS (cont'd) ZONE 2 Ex n DESIGN FIBERGLASS ENCLOSURE TYPE 4, IP66 GENERAL SAFETYLABEL-� [124,65mm] (8.49) 1215.68-1 08, I (217.O8nmj LCD DISPLAY I (f3f.75mmj� It2*FNPT (TYPICAL) SIGNAL (609) OUTPUTS I go" SENSORINPUTS (1.25)j57.15mnJ POMER INPUT AC OR OC I — (6.71) 0.31 [7.87-4 DIA THRU 1170.47t" 4x(TYPICAL) SENSOR ELECTRONICS FOR REMOTELY ATTACHED ELECTRONICS ENCLOSURE ITS) (WALL MOUNT) W/ DISPLAY & KEYPAD OPTION (SHOWN) (NOTES 3 & 4) 3,'4' 1,INPT 3x (TYPICAL) (28.70" ' (26.80mnj (SEETABLE2) (2.06) (52.32mnj 5.03 j127,76mm) I 5Z [I33.35mnj 4I [117.0 %9nn>) 4.37 MOUNTING FEET SU"ECTTO CHANGE SENSOR WIRE TERMINAL JUNCTION BOX (NOTE 2) (NOTE 3) CUSTOMER HOOKUP SIDE, &CONDUCTOR SHIELDED CABLE IN RIGID CONDUIT OR CABLE W9TH _ — — /-- PERIMETER BONDED SEAL BYCUSTO+AER 3'4'FNPT(TYPIKFLOW SAFETYAPPROVALT 3'4'MNPTPLUG CAUTION LABELZONE 1 ExdDESIGN GROUND LUGINIUM ENCLOSURE 8ID32SCRIWTYPE 4, IP66 OFLOWDIRECTIONARROW L)FLANGES(STANDARD) MN'(OPTIONAL) (SEE FEATURE 3) FLOW BODY ASSEMBLY FOR REMOTELY ATTACHED ELECTRONICS ENCLOSURE (TS) SHOWN (NOTES 1, 3, & 4) [127.76mm] 4.75 (120.65mnj 6.25 j13a35mmj 4.61 (117.09mnj 4.37 [110.99nvnj vo (SEETABLE2) (SEETABLE2) DUALCHAMBER ELECTRONICS ENCLOSURE (SHOWN W/WINDOW LID) (NOTE 3) 3'4' FNPT 3x (TYPICAL) one Thermal un, DRAWINGS (cont'd) SERIES 534FTB OUTLINE -- TABLE I-ENCLOSUREDIMENSIONS (l(1 (MAY -) INPUT pISPLAYI (p'') (PAIN.) W2 (IAIN.) GAIN.) POWER KEYPAD 3.63192.20mm1 5.01 I127�Smm1 NIA AC YES 3AI 186- 61mm] 4.691119.13mm1 5.011127�25mm] 3.16180_ 26n n1 _ NIA _ AC NO 2.81 [71.37mm] 4.691119.13mm1 3.63 [92.20mm1 5.01 [127.25mml NIA 24VDC YES 3.41186- 67mml 4b91119.13mm] 5.01(127�_ NO NIA NIA 4,881123.95mm1 24VOC (NOTE 41 3.16 (80.26mm1 SENSOR LANE NIA NIA 281[7137mm1- TERIJINALJ430X IAODEL NOMINAL I'Ll- NUMBER SIZE QNCHESI "'- (Li) L"I (L) 9.96(253.Dmm] 6.713.04 k91 8.2[3.72 kg] 9.2[4.17111 5MFT"A IR" 9.0 [228.6mm] 6.17[228.6mm] 6.B 13.08 k91 9.1 [4.13 k91 11.215.08 k91 FT8 3W �� 9. 11228.6mm1 6.17(228.6nnl 9.931253.Omm1 7.0 [3.17 k91 10.1 I4.58 k91 12.61531 k91 534FTB-06C 1° 9.01228.&-1 6.171228.6mm1 9.961253.Omm1 7.4 [3.36 kgl 8.914.04 k91 9.9110.3541 B34PTB-08A 1R° 15.01381.Umm] 6.23 [158.2mm1 9.961253.0mm1 7.613.45 k91 9.9 [10.35 kgl 12.015.44 k91 534FT&O88 3W 15A[381.Omm] 7,231183.6mm1 996 [253.Omm1 7.613.45 k91 10.7 (4.85 k91 13.2[5.99 k91 534FT8-0SC 1" 15.0(381.Dmm1 8.23 J209.0mm1 9.96 (253.Omm1 9.6 [4.35 kA] 11.9[5.40 kgl 14.0[6.35 41 534FTB-12A 314' 20.0[`508.�1 6.671169.4mn1 10.08 [256.Omm1 12.4 [5.62 kg] 14.9(6.76 k91 20.0(508.Omm] 7.54 [191.5mm1 10.08125&-1 9.314.22 k91 20.0[9.07 k91 53AFTB-12B 1° 9.981253.5mm] 10.081256��"] 9.9 [4.49 k91 15.0 (6.80 k91 534FTB-12C 1-17 20.0 [508.0nvn1 11.9 [5.40 kgl 15.0 [6.80 k91 17.5[7a4 k91 534FTB-16A 1' 26.0[660.4mm1 7.48[190.Omm) 10.211259.3mm1 16.9 7,6641 21.9[9.93 k91 [ 534FTB-16B 1-IR" 26.0(66 A-1 9.79[248.7mml 10.211259.3mm1 11.815.35 k91 20.5 (9.30 kg] 23.6 [70.70 kg] 2° 26.0 [660.4mm1 11.67 [296.4mm1 10.211259.3mmj 12.S 15.67 kq] 23.6 (10.70 k91 28.6 [12.97 kg] 534FT&16C 3B.01965.2mm] 4.00 (101.6mm] 9.28 (235.7mm] 18.5 [8.39 k91 29.9 [13.56 k91 534F7&24A b12" 9.28 [235.7mm1 18.8 [8.53 kg] 26.8 [12.15 k91 534FT&24B 21 38.0[965.2mm] 5.96 [151.4mm1 NIA 35.2 (15.96 kg] 42.6119.31 k91 534FT&24C 3° 38A 1965.2mml 10.75 [273.1mm1 928 (235.7mm1 26.6 [12.06 k91 34,6 [i5.69 kg] 37.7 [17.09 k91 5UFT032A Y 4g.011219.2mm] 4.87 [121.4mm1 9.54 [242.3mm] NIA 42.9 [19.46 kg] 50.3122.81 k91 534FT&32B 3° 48.011219.2mm1 9.521241.8mm] 9.541242.3mm1 49.0122�22 k91 66.7 [30.25 k91 4° 48.0 [1219.2mm1 13.681347.5mm] 9.541242.3mm1 NIA 72.4[32.83111 NIA SUFTB-32C 72.011828.Bmm] 7.18 [782.4mml 13.18 [33k&-1 NIA NIA 534FTB�BA 3" 13.18 [334.BWI NIA 78.6135.65 k91 534F76-48B 4• 11.24 [285.5mm1 72.D I1828.Bmm] NIA 87SI39.68 k91 NIA 534FTB-48C 6" 72.0 [1828.Bmm1 20.00 [5o.emml 13.16 (334.-1 NIA 122.61`�•`.60 k9) 94.0[2387.6mm1 9.18 (233.2mm1 13.18 [334.8mm1 NIA NIA 534FTB-64A 4" 17.82 [452.-1 13.18 [334.Bmml NIA 131.4159.60 k91 534FTB540 6° 94.0 [2387.6mm] NIA 151.9188.89 k91 NIA 94.0 [2387.6mm] 26.12 [663.411 13.18 (334.8mm] 534FTBS4C 8° NOTES'. 1)THIS PROBE CONFIGURATION ALSO USED FOR DIRECTLY ATTACHED, OC PONERED, NO DISPLAY' 2) SENSOR WTRETERMINIAL JUNCTION BOX USED FOR SENSOR ELECTRONICS FOR DC POWERED, NO DISPLAY. 3) ENCLOSURE STYLES AND DIMENSIONS ARE SUBJECTTO CHANGE. 41 THIS CONFIGURATIONS ALLOWS FOR PROBE ASSYTO BE MOUNTED IN ZONE 1 AR EAAND FOR REMOTE ELECTRONICS TO BE MOUNTED IN ZONE 2 AR 5) LDIMENSION IS OVERALL END TO END. 6) ADD 3.00 [762mm)TO LAND L1 DIMENSIONS FOR MNPT OPTION. 7) MIGHTS SHOMI ARE FOR DIRECTLY ATTACHED, AC POWER, WITH DISPLAY FOR REMOTELY ATTACHED VERSIONS ADD 4.0 LBS. [1.82 kg} " "'' """-`+��+-i�Sb • 831-646-5911' www.Kurzinstr'uments.com STANDARD FULL-SCALE FLOW RATES ESTIMATED PRESSURE DROP ° To compute the " - ' " • ' ' expected pressure drop for a now rate, multiply the full l scae pressure drop p by the square of the flow ratio. 534FT8- p6` 0.00045 81 12 534F r8-08 .6 10.8 0.00158 16,8 . • ' ' • • ° ' 28 534FTB-12 0.00341 44 31.2 58.5 -- 61 Air ° ° 534FTB-16 95 0.00590 -- - -126.4 ----- 106 .......81.1 -- - Arg._.__on_._.__-------- ..._._..._..7.5 _ ..._ 191 1.86 534FT6-24 -112 141 219.5 -�- .............._....... 534FT6-32 ----- 264 412 351.1 Butane --- _ --263 - - 2,56 __- 0.02454 442 548 534FTB-48 690 587.9 15.1 Carbon Dioxide 382 11.4 - 3.73 - 0.05642 1016 917.7 53--- 1585 4FT3-64 1351.3 Dry Ammonia -------------,-- __-289 ----"'- - ---- 4.4 i�- 2,83 0.09743 1754 ------------_._2108 ------......._ ........................_....__ ...........---.............__.. 2736 ........._........._..__2332.8 _ Dry Chlorine - --__ 112 1,09 ....................._...._.-__........_..........._............_..........._..............._....6................ 3638.9 Note: 18.4 Ethane 466 -----._________ 4.55 1. The baseline maximum flo------ rate for each transmitter model number. 2. Compressed air only. Ethylene 7'8 198 ---- _ ._._.-._. Helium 1.93 185......................................... 1.80 SCFM Standard Cubic Feet Per Minute, Reference: __ 1.0 ---- Hydro-- 9en 26 Methane 0 13 ...__...__..._ 0.26 77Y, 14.69 PSIA NCMH Normal Cubic Meters Per - _ Digester Gas: 500/o CHa, 0,13 Hour, Reference 0°C, 760 mmHg NCMH = ------............................._._........._- ..... x SCFM (approximate) 50% COz Digester Gas: 60%CHa, 198 1.03 _.................................__...................................... ._. _ 40% COz --- _ 7.1 Digester Gas: 70% CHa, 300, Coz 179 1.93 --- 1.75 Nitrogen --- 6'3 161 - 1.57 ......__......--- ----- - - _ Oxygen 7'3 184 ....... 1.80 1.80 _ 8.3 Propane - - ------__---210 2.06 11.4 290 2,83 _ Not ated pressure drop (DPs) is the end -to -end pressure drop _........................... standard conditions at at the baseline flow rate in Table A. 2411 Garden Road - Monterey, CA 939401800-424-7356. 831-646-5911 ( wwwXurzlnstruments.com 755 ~ — F7 FB Fg F10 Parent number F1 F2 F3 F4 FS F6 � � � — Inlet / Outlet Len th Parent Number Model Pipe Size 9 755439 534FTB-06B 0.75" 09 mm) 9" (229 mm)_ — 755440 534FTB-06c 1" (25 mm) 9" (229 mm) 755441 534FTB-08A 0.5" (13mm) 15" (381 mm) — 755442 —...---........... 755443 534FFB-08B --................. —......... _—._ 534FTB-08C 0.75"(19mm)- ......................15"(381 ............._........ .._......__ -- 1" (25 mm) mm) — 15"(381 mm) 755444 534FTB-12A 0.75" (19 mm) 20" (508 mm) 755445 534FTB-_12B 1" (25 mm) 20"(508 mm) — 755446 534FTB-12C 1.5" (38 mm) 20" (508 mm) 755447 534FTB-16A 1" (25 mm) 26" (660 mm) — 755448 534FTB-16B 1.5" (38 mm) 26" (660 mm) 755449 534FTB-16C 2" (51 mm) 26" (660 mm) 755450 _ _ 755451 534FTB-24A _ 534FTB-246 1.5" (38 mm) ......... 2" (51 mm) 38" (965 mm)...... . 38"(965 mm) 755452 534FTB-24C 3" (76 mm) 38"(965 mm) 534FTB-32A 2" (51 mm) 48"(1219mm) — _755453 755454 755455 534FTB-32B --- — -- ......._—.._ 534FTB-32C 3" (76 mm) .---.._...._....- 4" (102 mm) --48" (.1219 mm) 48" (1219 mm) 755459 534FTB-48A 3" (76 mm) 72" (1829 mm) --755460 755461 534FTB-48B 534FTB-48C 4"(102mm) ............_.......__.._72"(1829mm) ..... _ 6" (152 mm) 72" (1829 mm) 755462 534FTB-64A 4" (102 mm) 94" (2388 mm) 755463 53411-13-646 6" (152 mm) 94" (2388 mm) — 755464 534FTB-64C 8" (203 mm) 94" (2388 mm) Note: Model lengths from 9" to 48"use the MD sensor type. Model lengths 72- and 94"use the FD2 sensor type. Electronics Enclosure Configuration and Mimi I Input Power A Directly attached dual -chamber electronics enclosure, AC power, display / keypad B Directly attached dual -chamber electronics enclosure, AC power, without display / keypad _._-----._..._._..---.._....._....____ _-......_......._............_..._.._.....---....._............—.._......._—. C Directly attached dual -chamber electronics enclosure rotated 180° for viewing, AC power, display / keypad_-- Remote dual -chamber electronics enclosure, p AC power, display / keypad E Remote dual -chamber electronics enclosure, AC power, without display / keypad _ F Directly attached dual -chamber electronics enclosure, DC power, display / keypad-- ._..._....._.....---_—..... _......... --........ _....... - - Feature 1 (con't) G Directly attached dual -chamber electronics enclosure rotated 180° for viewing, DC power, display / keypad ..... _. FI Directly attached single -chamber electronics enclosure, DC power, without display / keypad -_ Remote dual -chamber electronics enclosure, I DC power, display / keypad Remote single -chamber electronics enclosure, DC power, without display / keypad R Remote polycarbonate electronics enclosure, AC/DC power, with display / keypad _...._—..__ .............._ ........ ._ ._.__._....._............._......---..__........._........_...........__....— - -- 5 Remote polycarbonate electronics enclosure, AC/DC power, without display / keypad — Remote stainless steel electronics enclosure, T AC power, with display / keypad Remote stainless steel electronics enclosure, AC power, without display / keypad _ Remote stainless steel electronics enclosure, W _ DC power, with display / keypad X Remote stainless steel electronics enclosure, DC power, without display / keypad Sensor& Flow Body Mate ial Choose one option from each category. 3 C-276 alloy 2 316L stainless steel A Male NPT pipe ends (MNPT) 300 PSIG B Class 150 ANSI B16.5 flanges (CL150) 150 PSIG — C Class 300 ANSI B16.5 flanges (CL300) 300 PSIG .. G DIN, PN 16, RF flang es 16 Bar 1 11S10K, RF flanges 10 kg/cm2 Standard temperature compensation over process range of -40°C to 125°C for all gases. 1 Accuracy: ± 0 + 2000 x A/F) %, where F = SCFM, A= flow body area (ft') -------- ......___..._..........—___.._............_.. Note: An accuracy specification of±0.025%/°C=(A•)(0.255FPM/°C) should be added for temperatures above or below standard. _ - - - • „ „— x :ccicy, vi ysJ4u I dUU-424-/356 < 831-646-5911I www.Kurzlnstruments.com F5 Gas Flow Rate Calibration Data Range Option Description Option I Description 11'. • 60 • may B 95%Qmax J 55%Qmax C ........... _............. --"-'—. 90%Qmax ....... _........_. _... -.---. K 50%Qmax D 85%Qmax L o _._...._.. 45 /o Qmax E 80%Qmax M 40%Qmax F -............ .-........ _..._. 75%Qmax ......... -..__....._.. -- ....—_ .... _........ N 35%Qmax G o %Q---- 70 max _.......... P ................................ ............. ...................... _.. 30 /o Qmax H 65%Qmax Q _ 25%Qmax Note: Refer toTables A and B to determine the correct selection for calibration range selection. •'IM Mffigimm� �1 ----------- 010 - Ambient Air 070 - Compressed Air - OKO Compressed Air (correlated to 4x baseline flow rate) 560 Dry Ammonia 080 580 Argon - 600 Butane 140 640 Carbon Dioxide - 680 Dry Chlorine 200 700 Ethane 220 60 720 760 Ethylene Helium 280 - Hydrogen 0 350 820 ........_......._ 850 Methane ........ -_........ -..... -- ...... _............. ...._....... Digester Gas 50 /o CH4 50% CO2 360 860 Digester Gas 60%CH4 40% CO2 370 870 Digester Gas 70%CH4 30% CO2 - ...................._._._.........----.._......._......._.-.. - 8K0 8MO User -Defined Binary Gas Composition —_......_._—_.._............. _............. One Gas Curve - 8NO Two Gas Curves -_ 800 Three Gas Curves - .-'-----_...........-._........ - 8PO -'-'--._......._ 8QO Four Gas Curves ... _........ ___.... _.._............ _........... Five Gas Curves 400 900 Nitrogen 440 940 Oxygen_ 460 960 Propane Notes, Laboratory gas calibrations are performed with high purity gases and are NISTTraceable. Customers must specify process pressure (Feature 8). Propane to 50 PSIA, all other gases to 150 PSIA. Options 8MO-8QO allow up to a 5-gas mix per curve; contact Kurz Sales Support if Hydrogen Is included in the mix. Non-incendive, CSA, ATEX, and IECEx Aluminum enclosure Type 4, IP66 Ex nA IICTx: Ex nA IIC Tx Gc; Class [Zone 2 AEx nA IIC Tx Gc A Sensing element, Tp: -40-C to 55'CTS or to 130-C:T3 DC power electronics housing,Ta: -40'C to 65'C:T4 AC power electronics housing,Ta: -401C to S0'C.'T4 or to 6S-C Ti 50'C CSA Approved for Class 1, Division 2, Groups B, C, D Explosion-Proof/Flame-Proof, CSA, ATEX, and IECEX Aluminum enclosure Type 4, IP66 Exd II8+H2T.; Exd 118+112T.Gb; Class (Zone 1 AEx d 118+H2TY Gb B Sensing element, Tp: -40-C to 45'C: T4 or to 110'C:T3 DC power electronics housing, Ta: -40'C to 65`CT4 AC power electronics housing, Ta: -40'C to SO'Ct'r4 or to 65"C T 150'C (f 3) .CSA Approved for Class 1, Division. 1, Groups B, C, D ......--_....-- —'- .—..._......_. Transmitter and sensing element separate Sensor enclosure: Aluminum Type 4, IP66 Electronics enclosure: Polycarbonate Type 4, IP54 (Feature 1, Option R or S) Sensing element: EXdl1B+H2Tx;Exdl18+H2TXGb;ClasslZonel AExdIIB+H2TxGb, D Tp:-40'Cto45'Ca T4orto110'6T3 AC power electronics housing: Ex nA IIC Tx ; Ex nA IIC Tx Gc; Class 1 Zone 2 AEx nA IIC Tx Gc,Ta: -25'C to SO'C: T4 Sensing element: CSA Approved for Class I, Division 1, Groups B, C, D Electronics housing: CSA Approved for Class I, Division 2, Groups B, C, D Remote -Transmitter and sensing element separate Sensor enclosure: Stainless Steel Type 4X, IP66 Electronics enclosure: Stainless Steel Type 4X, IP66 Explosion -Proof / Flame -Proof sensor: CSA, and IECEx H Exd II8+ 112T, Gb; Class l Zone i AEx d 11B+H2TxGb Sensing element, Tp: 40'C to 45'C: T4 or to I I WO T3 DC power electronics housing, Ta: -40'C to 65'C: T4 AC power electronics housing, Ta: 40'C to 50'C: T4 or to 65'C Tl SOT (T3) CSA Approved for Class r, Division 1, Groups B, C, D •Process Pressure Enter the Absolute Pressure (PSIA) rounded to 3 digits. - - - For example, a process Absolute Pressure of 14.7 PSIA, round to 15.0 and enter 015; for 150 PSIA enter 150, • • •Communications and Inputs/Outputs B Standard Two 4-2OmA isolated outputs --...........----.._ -- Two 4-2OmA isolated outputs, two relays, C Full two digital inputs, one non -isolated 4-2OmA input One 4-2OmA isolated output, two relays, E HART-1 two digital inputs, one non -isolated 4-2OmA input Two 4-20mA isolated outputs, two relays, H HART-2 two digital inputs, one non -isolated 4-2OmA input Two 4-2OmA isolated outputs, two relays, K Profibus DP two digital inputs, one non -isolated 4-2OmA _......... _........ _... ---............ ..._-- - .. •.Process Temperature Enter the Absolute Temperature (°Rankin ='F + 460) - - - , - rounded to a whole number. For example, a Process Temperature of 77'F is written as 0537 (77 + 460). Note: Add the letter'S"to the end of Feature 10 to include SILT certification. Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 Rosemount 1595 kosemount 1595 Conditioning Orifice Plate • Designed to provide superior performance in short straight pipe run applications • Requires only two diameters of straight pipe run after an upstream flow disturbance • Accurate and repeatable Comprehensive offering Suitable for most gas, liquid, and steam applications • Patent -pending technology Contents Rosemount 1595 Conditioning Orifice Plate ..... . Specification ................... . page 2 Dimensional Drawings............ page 3 Ordering Information ....................................................... page 5 Calculation Data Sheet " " " ' .... • , • page 8 Configuration Data Sheet (CDS) .. , , • . • • • ' ' ' ' ' ' ' . • • • • • •page 10 • • Fluid Data Sheet (FDS) .......... • . •................................. ' • • • page 11 ••••••page14 ROSEMOUNT' www.rosemount.com EMERSON- Process Manaoempnr Annubar Flowmeter Series: Rosemount 3051SFA, 3095MFA, 485, and 285 The state-of-the-art, fifth generation Rosemount 485 Annubar combined with the 3051S or 3095MV MultiVariable transmitter creates an accurate, repeatable and ies dependable ominsertional -type flowmeter. The Rosemount 285 provides a co offering for your general purpose applications. Compact Orifice Flowmeter Series: Rosemount 3051SFC, 3095MFC, and 405 Compact Orifice Flowmeters can be installed between existing flanges, up to a Class 600 (PN100) rating. In tight fit applications, a conditioning orifice plate version is available, requiring only two diameters of straight run upstream. Product Data Sheet 00813-0100-482806Rev EB Catalog 0 Rosemount 1595 Rosemount 1595 Conditioning Orifice Plate itionin Orifice Plate is designed to install downstream of a variety of disturbances with minimal The 1595 Cond g straight pipe run, providing superior performance. FIGURE 1. Rosemount 1595 Conditioning Orifice Plate 1595 Conditioning Orifice Plate based • A revolutionary innovative technology on the most common differential primary element in the industry • Requires only two diameters of straight pipe run after an upstream flow disturbance • Reduced installation costs • Easy to use, prove, and troubleshoot • Good for most gas, liquid, and tamas well as high temperature and high pressure applications 1595 Tailored Use The 1595 can be used in conjunction with the Rosemount 1496 Flange Union 11497 Meter Section. See Product Data Sheet nt 00813 0 00-4792 and Figure 2 and 3 for1496and number 1497 products. 0 O O 00 FIGURE 2. Rosemount 1496 Flange Union FIGURE 3. Rosemount 1497 Meter Section Rosemount DP -Flow Solutions Integral Orifice Flowmeter Series: Rosemount 3051SFP ProPlateO, 3095MFP Mass Proplate®, and 1195 These integral orifice flowmeters eliminate the inaccuracies that become more pronounced in small orifice line installations. The completely assembled, ready to install flowmeters reduce cost and simplify installation. Orifice Plate Primary Element Systems: Rosemount 1495 and 1595 Orifice Plates, 1496 Flange Unions and 1497 Meter Sections A comprehensive offering of orifice plates, flange unions and meter sections that is easy to specify and order. The 1595 Conditioning Orifice provides superior performance in tight fit applications. Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 Specification The Rosemount 1595 can be used with Rosemount 1496 Orifice Flange Unions and Rosemount 1497 Meter Sections. For product offering see document number 00813-0100-4792. Performance Flow Coefficient Uncertainty TABLE 1. Discharge Coefficient Uncertainty (3 - 0.20 ±0.50% R = 0.40' t0.50% R = 0.65 t0.75% (1) For 0.65 beta and ReD< 10,000 add an additional 0.5% to the Discharge Coefficient Uncertainty. Sizing Perform a flow calculation using the Instrument ToolkitT" software package. Alternatively, contact an Emerson Process Management representative. The "Configuration Data Sheet (CDS)" on page 11" is required prior to order for application verification. Straight Pipe Requirement Use the appropriate lengths of straight pipe upstream and downstream of the 1595 to minimize the effects of moderate now disturbances in the pipe. Table 2 lists recommended lengths of straight pipe, TABLE 2. 1595 Straight Pipe Requirements(l) 90° bend or tee Two or more 90° bends in different plane Reducer (1 line size) 2 --2-2 2 2 2' 2 2 2 2 , ;2 2;i 2 2 2 .• . 2 2 2; (1) Consult an Emerson Process Management representative if disturbance is not listed. Pressure Tap Orientation Orient the 1595 Conditioning Orifice Plate so that the pressure taps are centered between any 2 (of 4) orifice bore holes. Centering Requirements The 1595 should be installed so that it is centered in the pipes as recommended by ISO-5167. Functional Service and Flow Range Liquid, gas or vapor turbulent now, for pipe Reynold's Numbers greater than 5,000. For pipe Reynold's Numbers less than 10,000 add an additional +0.5% uncertainty to the discharge coefficient uncertainty, Rosemount 1595 Pipe Sizes 2 to 24-in. (50 to 600 mm). Contact Emerson Process Management for other pipe sizes. Operating Limits Temperature Range: -320 to 1200 °F (-196 to 649 °C) • - 320 to 800 °F (-196 to 427 °C) and differential pressure up to 800 inH2O • 800 to 1200 °F (427 to 649 °C) and differential pressure up to 400 inH2O Maximum Working Pressure • Flange rating per ANSI B16.5. Rosemount 1595 Physical Specifications Materials of construction Orifice Plate TABLE 3. S 316/316L A240 Gr S316001 1.4401/1.4404 SST 316/316L S31603 (1.4436/1.4435) L 304/304L A240 Gr S30400 / 1.4301 / 1.4306 SST 304/304L S30403 H Hastelloy B575 Gr N10276 2.4819 C-276 N10376 M ' Monet 400 B127 Gr', N04400 2.4360 N04400' Flange Mounting Hardware • The 1595 can be tailored for use in conjunction with the Rosemount 1496 Flange Union and, if required, the Rosemount 1497 Meter Section. See Figures 2 and 3 and Product Data Sheet 00813-0100-4792 for more information regarding the Rosemount 1496 and 1497. Typical Orifice Hole Sizes Beta is calculated by: (j3) = do / Pipe ID, where the calculated bore is equal to 2 x typical orifice hole size (d� = 2d). The table below shows the diameter of each of the four typical orifice holes. TABLE 4. 2-in (50.8 mm) 2.067-in. (52.502 mm) 0.207 (5.26) 0.307 (7.80) 0.413 (10.49) 0.614 (15.60) 0.620 (15.75) 0.997 (25.32) 34n. {76.2 mm) 3.068-in. (77.927 mm) 4.026-in. (102.26 mm) 0.403 (10.25) 0.805 (20.45) 1.308 (32.22) 4-in. (101.6 mm) 6-in. (152.4 mm) 6.065-in. (154.051 'mm) 0.607 (15.42) 1.213 (30.81) 1.971 (50.06) 8-in. (203.2 mm) 7.981-in. (202.717 mm) 0.798 nno ' 98 (0 dry 9 604 (50 90) 3.257 (82.73) 10-in. (254.0 mm) 12-in. (304.8 mm) 12.00-in. (304.8 mm) A� .200 (30.48; 2.946, 5 (6668) 4,265 (108.3; 14-in. (3550 mm) 13.250-in. (USn.eP n��,y ,� --,75(123.83) 16 -in . (406.4 mm) 15.250 in. (387.35 mm) 00 W1 W 3 00 c75 (85.73) 5.485 (139,32) 18-in. (457,2 Mm) ';17250-111. t4,50, I D'"1 ") •-•--, 20-in. (508.0 mm) 19.250 in. (488.95 mm) 1.n8n ids d8N 4 .762 525 (114 94) 7 353 {186.7 ) Orifice Type • Paddle, square -edge, concentric • Universal, square -edge, concentric Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 Dimensional Drawings 010 010 TABLE 5. Orifice Plate Dimensions in inches (millimeters) mm) (104.78 mm) 4.Si5-in. (111.13 mm 3. 3 (76.2 m) m 5.375 ' (136.53 mm) 5.875-i' (149n..23 mm 4-in. (101.6 mm) 6.875 074.63 mm) 7.125-in. (180.98 mm (1in.52 mm) 8.750 (2221-25 mm) 9.875-16. (250.83 mm; 8- 8-in., (203.2 mm) 11.000 (279.4 mm)I 12.125-in. (307.98 mm) 0-In. (254.0 mm) 13.375 (339.73 mm) 14.250-In, (361.95 mm) 12-in. mm) 16.125 (409.58 mm) 16.625-in. (422.26 mm) 14-in. (4-n. mm) 17.750 (450.85 mm) 19125-in, (485.78 mm); 16-In 16-in (406.4 mm) 20.250 (514.35 mm) 250-in. 21.mm) (539.75 39.75 18-in, mm) 21.500 (546.1 mm)' -in. ` (591725 mm) 205n2 (580.0 mm) tana �r50 „ 25.625-In. Rosemount 1595 Paddle Length Paddle Width (111.13 mm) 5.875-in. (142.875 mm �.�� 111. (142.875 mm) 5.75( (146.05 (14923 mm) 6.625-in. {i68.275 mm) 6.875-1n (i74.625 mm) 775C (196.85 7.125-in. (180.98 mm) 8.1254n. (206.35 mm) 8.250-in. (209.550 mm) 9.250 (234.95 10,5004n. (266 7 mm) 11.3754n. (288.925 mm) 11.125-in (282,575 mm) 12;50( 12.625-in. 320.675 mm) 14.125-in. (358.775 mm) 13.875-in. (317,50 15.25C 15.750-in. '400,05 17.125-16. (352.425 mm) 17,125-in (387.350 mm) (434.975 mm) (434.975 mm) 18.760 (476.25 18.000-in. (457,2 mm) 19.625-in. (498.475 mm) 20.500-In. (520.7 21.625 13.375-in. mm) (549.275 139.725 mm) 22.250-in. 565.15 mm) 24.000-in, 609,E mm) 26.750-in. 79.45 mm) TABLE 6. Orifice Plate Dimensions in inches (millimeters) �rrrs n•i 4-in. 4.406-in. (111.912 mm} 6-in, 6.4374n. (163.5'mm) I0I 8.437-in. (214.3 mm) 10n. 10.687-in, (271.45 mm) 12-in. 12.593-in. (319.862 mm) !b.4 mm) 11/4-in: 1.75 mm)` 11/4-in. 1.75 mm) 11/2-in.'. 8.1 mm) 1/2-in. 3.1 mm) 1/2-In. 1.1 mm) 1/2-in. 1 mm) 1/2-in, 1 mm) 1/2-in. .1 mm) /2-Im 1 mm) /2-in. 1 mm) NOTE Consult Factory for availability of line sizes not shown in the above table Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 Rosemount 1595 TABLE 7. Orifice Plate Dimensions in millimeters (inches) �N 50 (2-in.) • 107 (4.21) 107 (4.21) 107 (4.21) 107 (4.21) 142 (5.60) 113 (4.45) 148 (5.82) 119 (4.69) 154 (6.06) DN 80 (3-in.) 142 (5.60) 142 (5.6D) 162 (6.38) 142 (5.60) 168 (6.61) 168 (6.61) 174 (6.85) 180 (7.09) 257 (10.12) DN 100 (4-in.) DN 150 (6 in.) 162 (6.38) 218 (8.58) 218 (8.58) 224(8,82) 224 (8.82), 290 (11.42) 247 (9.72) 309(12. 09 (14.13) 324 (12.76) DN 200 (8-in.) 273 (10.74) 273 (10.74) 329 (12.95) 284 (11.18) 340 (13.39) 352 (13.86) 364 (14.33) 391 (15.39) 458 (18.03) DN 250 {10-in.) DN 300 (12-1n.) 328 (12.91) 378 (14.88) 384 (15.12) 400(15.75) flange 417 (16.42) 424 (16.69) ratings not shown in the above table. NOTE: Consult factory for availability of line sizes and 160 (6.299) 40 (1.575) 160 (6.299) 40(1.575)' 160 (6.299) 40 (1.575) 160 (6.299) 40 (1.575) 160 (6.299) 40 (1.575) 160 (6299) 40 (1.575) 160 (6.299) 40 (1.575) Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 TABLE 8. A.P.I Ring No.'s and Rating 02 R-23 02 300-600 R-24 02 900-1500 R-26 03 2500 R 31 03 300-600 & 900 R-35 04 1500 R-37 04 300-600 & goo R-39 06 ' 1500 R 45 06 300-600 & 900 R-46 08 1500 R-49 10 300-600 & goo R-53 300-600 & goo - NOTE Refer to Table 5 for line size and pressure rating availability. TABLE 9. Available Beta Ratio (p) The table below shows the available Beta Ratio <_ 80 2 0,20, 0.40, 0.60 2 160 0,20 3 XXs 0.20 3 s 80 0.20, 0.40, 0.65 3 160 0.20, 0.40 4 XXS 0.20 4 s 80 0.20, 0.40, 0.65 4 120 0.20, 040 4 160 0.20, 0.40 6 XXS < 0.20 6 80 0.20, 0.40, 0.65 6 120 ; 0.20, 0.40 6 160 0.20, 0.40 8 XXS 0.20 8 5 80 0.20, 0.40, 0.65 8 100 0.20, 0.40, 0.65 8 120 0.20, 0.40 8 - - 0.20, 0.40 8 160 0.20, 0.40 10 XXs 0.20, 0.40 10 < 80 0.40, 0.65 10 100! 0.20, 0.40, 0.65 10 120 0.20, 0.40 10 140 0.20, 0.40i 10 160 0,20, 0.40 12 XXs' 0,20, 0.40' 12 <_ 80 0.20, 0.40, 0.65 12 100 : 020, 0.40 12 120 0.20, 0.40 12 140 0,20, 0.40 12 160 0.20, 0.40 XXS 0.20, 0.40 < Rosemount 1595 12 14 R-57 300-600 & goo 14 R-61 300-600 16 R-62 900 16 R-65 300-600 18 R-66 900 18 R- 300-600 20 R-70 900 20 R-73 300=600 24 R-74 900 24 R-7:777 300-600 R-78 soo (p) for line size vs. pipe schedule 14 14 5 80 0.20, 0.40, 0.65 14 100: 0,20, 0,40 14 120 0.20, 0.40 14 140 0,20, 0.40 14 160 0.20, 0.40 16 XXS` 0.20,0.40 16 5 80 0.20, 0.40, 0.65 16 100 + 0.20, 0.40 16 120 0.20, 0.40 16 140 ' 0.20, 0.40 16 160 ' 0.20, 0.40 18 XXS 0,20, 0,40 18 80 0.20, 0.40, 0.65 18 100 0.20, 0,40, 0,65 18 120 0,20, 0.40 18 140 0,20, 0,40 18 160 XXS 0.20, 0.40 20 0,20, 0,40 20 80 0.20. 0.40, 0.65 20 100,0.20, OA0, 6.65 20 120 0.20, 0.40 140 0,20, 0,40 - 20 160 0.20, 0.40 24 XXS 0.20 0.40 24 80 0.20, 0.40, 0.65 100 0,20,i 0.40 - 24 120 0.20, 0.40 24 140 0.20, 0.40 24 160 0.20, 0.40 XXs 0.20, 0.40 Rosemount 1595 Ordering Information Rosemount 1595 Orifice Plate Ordering Table 1595 Conditioning Orifice Plate Square Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 020 2-in. (50 mm) 030 3-in. (76 mm) 040 4-in. (100 mm) 060 6-in. (150 mm) 080 8-in. (200 mm) 100 10-in. (250 mm) 120 12-in. (300 mm) 140 14-in. (350 mm) 160 16-in. (400 mm) 180 18-in. (450 mm) 200 20-in. (500 mm) D60) DIN PN 100 (only available with Plate Type P) R3 ANSI Class 300'Ring Joint (only available with Orifice Plate Type code U. and requires Plate Holder code PH) R6 ANSI Class 600 Ring Joint (only available with Orifice Plate Type code U and requires Plate Holder code PH) _ _- -.. - --I- I t --A ..,,�.d— Plata NnlriAr rnrle PHI ANSI Class 1500 Ring Joint (only available with Orifice Plate Type code U and requires Plate Holder code P DWI Stainless Steel C-276 0.125-in. (default for Line Sizes 2 to 4-in. (50 mm to 100 mm)) C 0.375-in. (default for line sizes 14 to 20-in. (350 to 500 mm)) D 0.500-in. (default for One sizes 24-in. (600 mm)) Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 Rosemount 1595 Orifice Plate Orderinn TAMP Q8 Material Certification per ISO 10474 3.1-13 and EN 10204 3.1.13 Code Conformance J5(5) NACE MR-0175 / ISO 15156 Country Certification J1 Canadian Registration (1) Currently available up to 12-in. (300 mm) line size. (2) Consult factory for availability of line sizes and flange ratings not shown. (3) PreviouslyPN64. Rosemount 1595 (4) For a Universal plate style in a 6-in. (150 mm) line size, the plate thickness is 0.125-in. (3.175 mm) and you will need to select code B. (5) Materials of Construction comply with metallurgical requirements within NACE MR0175/ISO for sour oil field production environments. Environmental limits apply to certain materials. Consult latest standard for details. Selected materials also conform to NACE MR0103 for sour refining environments. Rosemount 1595 Product Data Sheet 00813-0100-4828, Rev EB Catalog 2006 - 2007 Calculation Data Sheet This Calculation Data Sheet can be provided. The detailed sizing calculation may be done through the "Configuration Data Sheet (CDS)" on page 11. 1595 CONDITIONING ORIFICE PLATE CALCULATION DATA SHEET Customer: Customer Name Project: 2004 Official Calculations S. 0. No: Sales Order Number P. O. No: Customer Name Calc. Date: 4/7/2004 Model No: 1595POBOA3SBO40 Tag No: Tag Number Plate Type: Paddle, Square -Edged Tap Type: Flange tapping Upstream Plate Material: 316 SST Tap Location: Line Size: 8-in. (200 mm) (DN 200) Pipe Schedule: 40 Process Connection: Pipe Material: Carbon Steel Fluid Type: Steam Calibration Factor: 1.000 Fluid Description: Pipe I.D.: 7.981 60,000023 inch psig Base Pressure Pressure: Temperature at Flow: 307.33 F Base Temperature Absolute Viscosity: 0.01409 cP Isentropic Exponent: 1.31746 Base Compressibility Compressibility at Flow: 0.171328 Ib/ft3 Base Density Density at Flow: Atmospheric Pressure: 14.696 psia Flow Rates: Minimum: 6000.00 Ib/hr Normal: 8000.00 lb/hr Maximum: 10000.00 Ib/hr Full Scale: 10000.00 Ib/hr a cu ation pe orme at norms con i ions Bore Reynolds Number (Normal): 1120650 Orifice Bore Size: 0.596 inch inch Pipe Reynolds Number (Normal): 448514 Orifice Effective Bore Size: 3.192 42.859 in H2O at 68 °F Gas Expansion Factor: 0,9900 DP at Minimum Flow: DP at Normal Flow: 76.194 in H2O at 68 °F Permanent Pressure Loss: 62.671 in H2O at 68 °F DP at Maximum Flow: 119.054 in H2O at 68 °F °F at Normal Flow: Max Flow: 97.928 in H2O at 68 °F URV (DP at Full Scale): 119.054 in H2O at 68 at Velocity at Max. Flow: 46.669 ft/sec Beta: 0.400 0.6009 Minimum Accurate Flow: 1313.27 Ib/hr Discharge Coefficient: °F Max. Allow. Pressure at Temp: 555.500 psig @ 310 Gas Expansion Factor Notice at Normal Flow. Calculation by HL terms Version: 3.0 (Build 1 Printed on: 10 More information and current pricing: www.endress.com/5W3B Products Solutions Services Proline Promag HIV 300 electromagnetic flowmeter Specialist for demanding water & wastewater applications with compact, easily accessible transmitter Benefits: ■ Reliable measurement at constant accuracy with 0 x DN inlet run and no pressure loss oint rocess ■ Flexible engineering — sensor with welded or lap-j p connections • Long-term operation — robust and completely welded sensor ■ Improved plant availability — sensor compliant with industry -specific requirements • Full access to process and diagnostic information — numerous, freely combinable I/Os and fieldbuses ■ Reduced complexity and variety — freely configurable I/O functionality . intPnrated verification — Heartbeat Technology Endres+Hauser ID Proline Promag W 300 / 5W3B Field of application: The premium device for water and wastewater measurement Promag W 300 was designed for reliable use in hazardous areas and under harsh conditions. Its compact transmitter offers high flexibility in terms of operation and system integration: access from one side, remote display and improved connectivity options. Heartbeat Technology ensures measurement reliability and compliant verification. Features and specifications ---- ---------- squids _ - ----- - Measuring principle --- Electromagnetic Product headline Specialist for demanding water and wastewater applications with a compact, easily accessible transmitter. Reliable measurement at constant accuracy with 0 x DN inlet run and no pressure loss. Dedicated to the measurement of industrial or municipal water and wastewater. Sensor features Flexible engineering — sensor with fixed or lap joint process connections. Long-term operation — robust and completely welded sensor. Improved plant availability — sensor compliant with industry -specific requirements. International drinking water approvals. Transmitter features Full access to process and diagnostic information — numerous, freely combinable I/Os and fieldbuses. Reduced complexity and variety — freely configurable 1/0 functionality. Integrated verification — Heartbeat Technology. Compact dual -compartment housing with up to 3 I/Os. Backlit display with touch control and WLAN access. Remote display available. Nominal diameter range DN 25 to 3000(1 to 120") 2 Endres.+NA„enr Proline Promag W 300 / 5W3B Liquids Wetted materials Liner: Polyurethane; Hard rubber, PTFE Electrodes: 1.4435 (316L); Alloy C22, 2.4602 (UNS N06022); Tantalum Measured variables Volume flow, conductivity, mass flow Max. measurement error Volume flow (standard): ±0.5 % o.r. ± 1 mm/s (0.04 in/s) Volume flow (option): ±0.2 % o.r. ± 2 mm/s (0.08 in/s), Flat Spec Measuring range 0.5 m3/h to 263000 m3/h (2.5gal/min to 1665 Mgal/d) Max. process pressure PN 40, Class 300, 20K Medium temperature range Liner material hard rubber: 0 to +80 °C (+32 to +176 °F) Liner material polyurethane: —20 to +50 °C (-4 to +122 °F) Liner material PTFE: —20 to +90 °C (-4 to +194 °F) Ambient temperature range Flange material carbon steel: —10 to +60 °C (+14 to +140 °F) Flange material stainless steel: —40 to +60 °C (-40 to +140 °F} Sensor housing material DN 25 to 300 (1 to 12"): AISi10M9, coated DN 25 to 2400 (1 to 90"): Carbon steel with protective varnish Sensor connection housing (standard): AISi10Mg, coated Sensor connection housing (option): Polycarbonate; 1.4409 (CF3M) similar to 316E Transmitter housing material AISi10M9, coated; 1.4409 (CF3M) similar to 316L; stainless steel for hygenic transmitter design Endress+Hauser q Proline Promag W 300 / 5W3B Liquids Display/Operation 4-line backlit display with touch control (operation from outside) Configuration via local display and operating tools possible Remote display available Outputs 3 outputs: 4-20 mA HART (active/passive) 4-20 mA WirelessHART 4-20 mA (active/passive) Pulse/frequency/switch output (active/passive) Double pulse output (active/passive) Relay output Inputs Status input 4-20 mA input Digital communication - --- HART, PROFIBUS DP, PROFIBUS PA, FOUNDATION Fieldbus, Modbus RS485, Profinet, Ethernet/IP, OPC-UA .-.....- .... Power supply DC24V AC100to230V AC 100 to 230 V / DC 24 V (non -hazardous area) Hazardous area approvals ATEX, IECEx, cCSAus, Nepsi, INMETRO, UK Ex Product safety CE, C-tick, EAC marking Functional safety Functional safety according to IEC 61508, applicable in safety -relevant applications in accordance with IEC 61511 4 Fn1grno 1_LT Proline Promag W 300 / 5W3B Metrological approvals and certificates Liquids Calibration performed on accredited calibration facilities (acc. to ISO/IEC 17025), NAMUR logy complies with the requirements for measurement Heartbeat Techno traceability according to ISO 9001:2015 -Section 7.1.5.2 a (TUV SOD attestation Marine approvals and certificates LR approval, DNV GL approval, ABS approval, BV approval Pressure approvals and certificates CRN, PED Material certificates 3.1 material _ Hygienic approvals and certificates ACS, KTW/W270, NSF 61, WRAS BS 6920 More information www.endress.c0m/5W3B addresses.endress.com Endress+Hauser AG info@endress.com Endress+Hauser 10 0 z R11}?363?5 .Y�N1` itthT] t103 Y3yY JYO �� vain 4 iano � �� __- -. r-YLL Y3nvJYnYyt rige } F r �� b3ravxs3ani�n� n - : •8i ry SI YiYNA) ¢ X rhYt03; Zyn i DN U3tY?H �X � h:n zos �R a� ones 09, ��i nnn rrr i vk 11Nn tr3N3:A SJ+12153U.3+aJTP i( 3;Y+u1 i 'N 1N1ry � yY�py3 ixwtsat 31nTc qq 2dt�YUliJ 5= 3� TJSVi? 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( � \ \ \ B ; § § �k �2 --- »a � ®- - - - - - - - -� y�w » ( � � § % , | \ a ° - ---------------------------- q �) »6 ye_ E 7 No om I $ e> ` e_ Me/ ` ( ] ee / ! , ƒJ- 2 �� \ @/ % B A \ \ \ \ I \ § 0 % 0 I �-S- 0\\ m�° z / oso3 a M M O I \ a \ \ I See Chapter A - 2 See Chapter 2.4 - Control Narrative See Chapter 2.3.3.3 - PSU Schematic Drawing See Chapter 2.4 - Control Narrative Printed: 2023-10-11 Ozone System Control: Functional Design Specification TABLE OF CONTENTS 1 USUAL ABBREVIATIONS........................................................................................................................ 2 PROCESS OVERVIEW.................................. ..............................................................................................................2 3 CONTROL SYSTEM HARDWARE................................................................................................................................3 4 GENERAL CONTROL CONCEPTS..............................................................................................................................5 4.1 REMOTE / LOCAL ............................. •2 INTERLOCKS, ALARMS AND WARNINGS •°•••••••••••5 4.3 COMPONENT AUTO / MANUAL / OUT-OF-SERVICE..............................................................................................5 •4 EQUIPMENT PRIORITY AND ROTATION ............................................................................. 5 ......................... 4.5 GAS FLOW MEASUREMENT AND CORRECTION .......................... 4.6 CLOSED -LOOP CONTROLLERS .............................. ..............................°...................................................5 .6.1 Controllers Interface........................................................................................................ .............6 .......................................... 4.7 PLC COMMUNICATION MONITORING .............................6 .......................... ...... .......................................................................... 7 5 OZONE PRODUCTION CALCULATION OVERVIEW 5.1 REQUIRED OZONE DEMAND ................... ..................................................................................................8 .2 INITIAL GAS FLOW REQUIREMENTS 8 ............................................ 5.2.1 Ozone Contactor Gas Flow Sizing """""' 8 2.2 Ozone Contactor Gas Flow Low Limit 9 .......................................... 5.2.3 Ozone Contactor Gas Flow High Limit ............................................................................................................10 5.3 OZONE -IN -GAS CONCENTRATION SET POINT ............. 5.3.1 Plant Gas Flow Low Limit .................. . 5.4 FINAL GAS FLOW REQUIREMENTS 10 ...................................... .....................................................................................11 5.5 CONSTANT GAS FLOW MODE VS. VARIABLE GAS FLOW MODE 6 PERFORMANCES MONITORING................................................................ .................................•,,,,,,,,,,,,, 11 6.1 OZONE GENERATOR PRODUCTION ........................ 7 OZONE SYSTEM OPERATING SEQUENCE..............................................................................................................13 MAIN COMMANDS............... 77.1 .2 INTERLOCKS & PERMISSIONS.................................................................................................................................13 .......,,.,........................................................................................13 7.2.1 Generator Permissive....................................................................................... 7.2.2 Generation Safety y............................................................................................................................................13 13 7.2.3 Global -Trip Interlock (GTI)...............................................................................................................................13 Ambient -Trip Interlock(ATI).............................................................................................................................13 77.2.4 .2.5 Slow -Trip Interlock (STI)..................................................................................................................................13 7.3 SEQUENCE STATUS DISPLAY ............................................... START-UP SEQUENCE.............................................................................................................................................14 14 7.4 .5 SEQUENCED SHUT-DOWN.......................................................................................................................................15 7.6 IMMEDIATE SHUTDOWN ............................... 8 LOX STORAGE SUB-SYSTEM...................................................................................................................................16 ...............15 8.1 ALARMS WITH EFFECTS.......................................................................................................................................... 8.2 SUBSYSTEM "NOT AVAILABLE" ..................... .16 .3 SPECIFIC SUB -SYSTEM CONTROLS...........................................................................................................................16 16 9 VAPORIZER SUB-SYSTEM........................................................................................................................................17 ALARMS WITH EFFECTS...........................................................................................................................................17 99.1 .2 SUBSYSTEM "NOT AVAILABLE"....................................................................................................................... 9.3 SPECIFIC SUBSYSTEM CONTROLS..............17 9.3.1 Priority Selection, Rotation and Demand.........................................................................................................17 17 10 OXYGEN FEED GAS MONITORING AND CONTROL 10.1 ALARMS WITH EFFECTS .......................................... ................................................ 10.2 SUBSYSTEM "NOT AVAILABLE" 18 10.3 SPECIFIC SUB -SYSTEM CONTROLS 19 ...........................................................................................................................19 11 NITROGEN SYSTEM...................................................................................................................................................20 11.1 ALARMS WITH EFFECTS ....................... File: Q121033MPo1nnnn rinev _ . . Ozone System Control: Functional Design Specification P. ii Printed: 2023-10-11 11.2 SUBSYSTEM "NOT AVAILABLE..................................................................................................................................20 11.3 SPECIFIC SUB -SYSTEM CONTROLS ............................................... 12 OZONE GENERATION SUB-SYSTEM.......................................................................................................................21 .......,.... 22 12.1 ALARMS WITH EFFECTS...........................................................................................................................................22 12.2 SUBSYSTEM "NOT AVAILABLE' ................................... ..............................22 12.3 SPECIFIC SUB -SYSTEM CONTROLS...........................................................................................................................2 12.3.1 Priority Selection, Rotation and Demand... ........................................................................ 13 COOLING WATER SUB-SYSTEM..............................................................................................................................23 13.1 ALARMS WITH EFFECTS............................................................................................................... .......24 13.2 SUBSYSTEM "NOT AVAILABLE"............................................................................................................. 13.3 SPECIFIC SUB -SYSTEM CONTROLS...........................................................................................................................24 .......24 13.3.1 Priority Selection, Rotation and Demand.................................................................................................. 14 OZONE CONTACTOR SUB-SYSTEM........................................................................................................................25 14.1 ALARMS WITH EFFECTS..................................................................... 25 14.2 SUBSYSTEM "NOT AVAILABLE"........................................................................................................... ..................... ...............26 14.3 SPECIFIC SUB -SYSTEM CONTROLS ............................... ........2 14.3.1 ONLINE/OFFLINE State.......................................................................................................................... 15 OZONE DESTRUCT SUB-SYSTEM............................................................................................................................27 15.1 ALARMS WITH EFFECTS................................................................................................................................... ..........28 15.2 SUBSYSTEM "NOT AVAILABLE'.................................................................................................................................28 15.3 SPECIFIC SUBSYSTEM CONTROLS................................................................................................................. 15.3.1 Priority Selection, Rotation and Demand ................... ............................... AND EMERGENCY SHUTDOWN SUB-SYSTEM.......................................................29 16 AMBIENT GAS DETECTION ...........29 16.1 ALARMS WITH EFFECTS................................................................................................................................ 16.2 SUBSYSTEM "NOT AVAILABLE"................................................................................................................................29 16.3 SPECIFIC SUB -SYSTEM CONTROLS...........................................................................................................................29 Doc. Q121033-MP-010 Rev.2 rrinted: 2023-10-11 Ozone system Control: Functional Desi n Specification 1 USUAL ABBREVIATIONS 1 of 2s The following standard abbreviations and designations are used throughout the entire project documentation Al = PLC Analog Input AO = PLC Analog Output DI = PLC Digital Input DO = PLC Digital Output CPU = PLC Central Processor Unit DCS DH = Distributed Control System and/or Plant operator workstations OIT = = Data Highway (PLC Data link in a Network configuration) 1/0 Human Machine Interface (for Master PLC) = LOX PLC Input/Output = Liquid Oxygen System MCB = Microprocessor Control Board MCC = Motor Control Center MOCP = Ozone Master Control Panel ODCP = Ozone Destructor Control Panel ODU — Ozone Destruct Unit OGCP = Ozone Generator Control Panel OIT = OMI Local Panel Screen Type Operator Interface Terminal = OXGCP = Operator -Machine Interface (see OIT) PLC Oxygen Generator Control Panel = PSU Programmable Logic Controller = RIO Power Supply Unit = ROCP = Remote 1/0 Remote ozone Control Panel RTU = Remote Terminal Unit SCADA = UPS Supervisory Control and Data Acquisition = VOD Uninterruptible Power Supply = Vent Ozone Destructor (see ODU) File: Q1210IRMPninnnn a Printed 2023 10 11 Ozone System Control: Functional Design Specification p. 2 of 29 PROCESS OVERVIEW By means of an electrical discharge, ozone (03) is produced by splitting Oxygen (02) molecules into Oxygen atoms (0) which when combined with non -split Oxygen molecules form an ozone molecule (03), i.e., "02 + 0 = 03". Ozone is an extremely strong oxidizing agent but is unstable and spontaneously degrades back into oxygen. Therefore, it cannot be stored and must be produced on site just prior to use. Gaseous Oxygen is obtained by the evaporation of liquid Oxygen (referred to as LOX), stored in on site in one or more LOX tanks. Liquid oxygen is evaporated using an evaporation system that includes at least one vaporizer. The vaporizer's discharge is piped to a header, also called the GOX Header. To improve the efficiency of the ozone generation process, a small amount of Nitrogen must be added to the Oxygen, upstream of the ozone generator. The Nitrogen is essential for proper operation of the generator dielectrics and although the system will allow limited operation when little to no nitrogen is introduced (maximum power at the generator vessel is 50% in this case), long-term operation of a generator without any nitrogen at all is not recommended. The required nitrogen is obtained by compressing and drying ambient air, and injecting it at a controlled rate into the Oxygen stream (GOX header). Ozone is produced inside a vessel referred to as the ozone generator vessel, by means of a high voltage alternating current applied between two electrodes separated by a gap through which the Oxygen flows. One of the electrodes is covered with a ceramic coating, as known as the dielectric. The generator's stainless steel shell acts as the other electrode. The ozone generator package includes monitoring and interlocking instrumentation to safely produce ozone. This package includes a power and control cabinet (referred to as PSU), an Oxygen inlet line, an ozone discharge line, and a cooling water system. After generation, ozone is fed into a dissolution system, where ozone -rich gas is introduced into water needing to be treated. The remaining non -dissolved ozone is evacuated through the off -gas line. Ozone in the off -gas line is recuperated by means of at least one vacuum blower. The ozone -rich (in low -concentration) gas flows through a catalytic chamber which is used to neutralise any remaining ozone. This package (blower and catalyst) is better known as the ozone destruct unit. Multiple ambient monitoring devices monitor gas leaks. These will be located throughout the ozone plant in strategic locations and all will be used by the ozone control system in order to maintain a safe operating environment. Major gas leaks will shut down either portions of or the entire ozone system. Film 01210331MP010000.dou Oshkosh WFP Doc. Q121033-MP-010 Rev.2 Printed: 2023-10-11 Ozone System Control: Functional Design S ecification . 3 of 29 3 CONTROL SYSTEM HARDWARE The ozone system and associated components and controls include, but are not limited to: The Master Ozone Control Panel (CP-PLC-D, aka MOCP). The major components of this panel are: o A programmable logic controller o An operator interface terminal • Two (2) typical LOX Unloading Panels (LCP4004A, LCP4004B) Panels are not equipped with local PLCs or OITs. Panels are wall -mounted type, installed outside, near the LOX storage tanks. All wiring from the LOX tank instruments are wired to this local control panel. Panel is equipped with indicating lights, horn and strobe. • Three (3) Power Supply Units (M4130-2/3/4, aka PSU #2/3/4). Each PSU is made up of. o A mains power section o One or more Power Stages (providing power to the ozone generator), each made up of: ■ A power electronic section, containing a power converter/inverter module ■ A high voltage section, containing a high -voltage transformer o A control section, which is described as the Ozone Generator Control Panel (LCP4131-2/3/4, aka OGCP #2/3/4). The major components of this panel/section are: ■ A programmable logic controller ■ An operator interface terminal • Three (3) sets of Destruct Panels There are two (2) unique panels per Ozone Destruct Unit. Neither of the two (2) panels are equipped with local PLCs or OITs. Both panels are mounted on the Ozone Destruct skid. o Ozone Destruct Local Control Panel (LCP4501-1/2/3, aka ODLCP #1/2/3) All wiring from skid -related instruments that are single-phase voltage (120VAC, 24VDC), such as valves, sensors, and limits switches, are wired to this local control panel. Panel is equipment with relays, terminals, and fuses. The main component of this panel is: o A door -mounted temperature controller, controlling power to the pre -heater. o Ozone Destruct Power Panel (LCP4502-1/2/3, aka ODPP #12/3) All wiring from skid -related equipment that are three-phase voltage (480VAC), such as valves, heaters, and blowers, are wired to this local control panel. This panel is equipment with motor starters, terminals, and fuses. The main components of this panel are: o An internal variable frequency drive (VFD) providing power to the vent -gas blower o A power modulating device providing power to the pre -heater • One (1) set of Nitrogen Panels File: Q1210331VIP010000.doa Oshkosh VVFP M-- 4 A,,,,,, - Printed 2023 10 11 Ozone System Control: Functional Design Specification p. 4 of 29 There are two (2) unique panels for the Nitrogen Generation Unit. Neither of the two (2) panels are equipped with local PLCs or OITs. Both panels are mounted on the Nitrogen Generation skid o Nitrogen Generator Local Control Panel (LCP4902, aka NGLCP). All wiring from skid -related instruments that are single-phase voltage (120VAC, 24VDC), such as valves, sensors, and limits switches, are wired to this local control panel. This panel is equipment with relays, terminal, and fuses. The major component of this panel is: o An alternating relay for compressor operation o Nitrogen Generator Power Panel (*LCP4902A, aka NGPP) All wiring from skid -related equipment (compressors) that are three-phase voltage (480VAC) are wired to this local control panel. This panel is equipment with motor starters, terminals, and fuses. The main components of this panel are: o An internal variable frequency drive (VFD) providing power to the vent -gas blower o A power modulating device providing power to the pre -heater • Two (2) unique Alarm Panels (provided by others) There are two (2) unique panels. Neither of the two (2) panels are equipped with local PLCs or OITs. Both panels are wall mounted. o Ozone Generator Room Alarm Panel (LCP4635) All wiring from field instruments that are single-phase voltage (120VAC, 24VDC), such as ambient analyzers, emergency stop stations, strobes, and horns (to name a few) are wired to this local control panel. Panel is equipment with relays, terminals, and fuses. This panel interfaces with ventilation -related equipment. o Ozone Gallery Area Alarm Panel (LCP4640) All wiring from field instruments that are single-phase voltage (120VAC, 24VDC), such as ambient analyzers, emergency stop stations, strobes, and horns (to name a few) are wired to this local control panel. Panel is equipment with relays, terminals, and fuses. This panel interfaces with ventilation -related equipment. rlehknch WFP Doc. Q121033-MP-010 Rev.2 Printed: 2023-10-11 Ozone System Control: Functional Desi n Specification . 5 of 29 4 GENERAL CONTROL CONCEPTS As a general statement, a component is totally controlled and monitored from the control panel (with or without PLC) to which its instruments are wired; interlocks, alarms, shutdown logic and closed -loop controls are all done locally. Detailed alarms are also enunciated locally, either via an OIT or simply through panel mounted pilot lights. 4.1 REMOTE / LOCAL Most components (valves and motors) are equipped with a local control box containing a LOCAL -REMOTE selector switch and local operation push buttons or switches. Just like a valve or a pump, a local control panel will also have its own LOCAL -REMOTE selector, either by a physical switch on the panel or via button selectors on a local operator interface. The REMOTE mode may be selected at any time. LOCAL selection allows for operation from the local control panel. In the REMOTE mode, the unit is started and stopped from the remote -control unit (local or master control panel). 4.2 Interlocks, Alarms and Warnings Alarms are displayed through the OIT integral alarming system. Some alarms are continuously monitored, whereas others are only monitored when required (ex: a low pressure at a pump discharge is not monitored when the pump is not running). All alarms are configured latched, where they require a reset or clearing action. An alarm remains enabled until the cause of this alarm has disappeared, and the operator has pressed the clear/reset command at the interface. Local control panels with PLC and OIT have their own alarm acknowledge. Alarms are all configured as latched alarms. In the case of a PLC -equipped panel, a single reset is sent from the Master Control Panel to acknowledge the alarms remotely. Some alarms are only warnings whereas others are part of either plant shutdown sequences or equipment interlocks. For a list of ozone -plant -level interlocks and permissions, please refer to section 7.2 (Interlocks & Permissions). 4.3 Component AUTO / MANUAL / OUT -OF -SERVICE All devices (pumps, valves, ozone generators, ozone Destruct units, etc.) may be globally selected by the operator from the OIT as being in AUTO, MANUAL or OUT -OF -SERVICE. A device in AUTO means that the unit is available for the automatic sequencing. To operate manually, operator must select MANUAL. When placed in OUT -OF -SERVICE, the device is locked -out, in most cases for maintenance purposes. A unit operates in auto mode if: • The switch on the device is placed in REMOTE • It is selected to AUTO For parallel devices (ozone generators, ozone destruct units, pumps) at least one unit must be selected in auto or manual to operate the system in accordance with the facility start/stop logic. In the event all parallel devices are in offline mode, the sub -system the devices belong to will interlock and may cause train or complete plant shutdown. 4.4 Equipment Priority and Rotation All parallel devices (ozone generators, ozone destruct units, valves, etc.) may be selected as LEAD, LAG1, LAG2, etc via commands at the operator interface(s). Additionally, some parallel devices will also include an automatic timed rotation feature. Rotation of the devices will occur only if the feature is enabled and at the end of the elapsed time, as set by the operator. File: Q1210331VIP010000.docx n�nk �h �niro Printed: 2023-10-11 Ozone System Control: Functional Design Specification . 6 of 29 4.5 Gas Flow Measurement and Correction Where flow measurement is done, temperature and pressure measurements are usually also done. The correction depends of the flowmeter type; for a differential pressure type flowmeter (like orifice plate, venture), the correction is: FACT — F xr�CCA xTACTCAL Where FACT = Flow Reading at actual pressure and temperature conditions (in SCFM) F = Flow Reading as read by the flowmeter at calibration conditions (in SCFM) PACT = Actual absolute pressure (in psia; psig + 14.7) PCAL = Flowmeter calibration absolute pressure as per flowmeter specifications. TACT = Actual absolute temperature (in OR; OF + 460) TCAL = Flowmeter calibration absolute temperature as per flowmeter specifications. For a linear -type meter (like vortex -type), the correction is linear: FACT = F x PACT x TcAL PCAL TACT In order to avoid false readings of the actual gas flow, when a pressure transmitter fails (out -of -range), the pressure correction factor is forced to 1; in the same way, when a temperature transmitter fails, the temperature correction is forced to 1. In the event the instrument is one that already takes these values into consideration, the above -mentioned formula does not apply. The conversion between the volumetric flow (SCFM) and mass flow (Ibs/day or PPD) is done by: FALAss = 1440 x p x F,oL Where FMASS= Gas mass flow (in Ibs/day or PPD) p = Gas density at STP (in Ibs/ft3) FACT = Volumetric flow (in SCFM) 4.6 Closed -loop controllers 4.6.1 Controllers Interface Whenever is required to control a process variable (PV) by maintaining a certain setpoint (SP) through an equipment position (CV). A PID (Proportional -Integral -Derivative) algorithm will be provided. The control modes and configuration parameters will be available from the screen. Except where noted, the interface for these controllers includes: ci... n,oanwnnpnlnnnn rincx Doc. 0121033 MP-010 Rev.2 Oshkosh WFP Printed: 2023-10-11 Ozone System Control: Functional Design Specification . 7 of 29 • AUTO -MANUAL selection: in AUTO, the controller is in closed -loop and any combination of the PID algorithm is used to maintain the process at the setpoint value (SP). In manual (open loop mode), the controller output is an operator -entered value. When switching from auto to manual, the output keeps the last auto value until the operator changes it. Status of this selection is shown at interface. • Optional OPERATOR -CALCULATED selection for the set point. This option gives to the user the opportunity to use for the controller set point either a value provided by the control system (CALCULATED set point) or a manually entered value (OPERATOR set point). Status of this selection is shown at interface. • The controller contains an "Enable" signal; when controller is disabled, the output turns to 0 • Actual controller Set Point value (SP) either entered by the OPERATOR or the result of a CALCULATED value. The process variable (PV), feedback signal and Actual Output value (CV) are also displayed. • In some instances, the controller's control value (CV) is used to provide a «trim factor» on a process variable. The standard 0 to 100 % range of the control value is re -ranged to a —100.0 to +100.0 %. When this type of controller is disabled, its output is forced to 0, which represent 1.0 or a factor of NONE. When it is enabled, the output varies between —100.0 to +100.0 % and is introduced as a multiplying factor in the control system once rescaled. The rescaled CV can be whatever the process being controlled can accommodate for. • As mentioned in the previous point, the control value can also provide "trim factoring" behaviour on another CV, one that is the result of a feed -forward or biasing function. 4.7 PLC communication monitoring To monitor the PLC communication between PLCs, a single bit heartbeat pulse (20 seconds ON, 20 seconds OFF) is generated in each PLC unconditionally. The receiving PLC monitors the pulse continuously. If the received heartbeat remains ON or OFF for more than 40 seconds, an alarm "COMMUNICATIONS FAILURE" is displayed. Once the alarm is generated, all data received from the remote PLC will be forced to "0" and reset. For the "receiving" PLCs, this means that if any interlocking conditions are passed over the communication link, the "receiving" panel/PLC will be interlocked, and in most cases, will shutdown its controls. The "sending" PLC will force the associated device into Offline mode. The pulse and alarm time noted here are typical and may be changed and adjusted, in relation with the network response time during start-up and commissioning. File: Q121033MP010000.docx Oshkosh WFP Printed 20231011 Ozone System Control: Functional Design Specification p. 8 of 29 5 OZONE PRODUCTION CALCULATION OVERVIEW 5.1 Required ozone Demand The control system will calculate the required ozone demand for each ozone contactor individually: PDCTX = k x QcTx x DsP Where PDCTx = Required ozone Demand for a given ozone contactor (in Ibs/day) QcTx = Raw Water Flow for a given ozone contactor (in MGD). DsP = Dosage Setpoint for a given ozone contactor (in mg/I) k = unit dependent factor (8.345) The Raw Water Flow rate per contactor is calculated as follows: QT QcT` _ �` CONT !� ONLINE Where QT = Total Raw Water Flow in the Plant (in MGD). CONTom iNE = Number of Contactors ONLINE (in Service) in the plant The total required ozone demand for the entire system is the sum of all required ozone demands: PD = I PDCTz Where PD = Required ozone Demand for entire plant (in Ibs/day) The plant ozone demand is utilized further, in determining the exact gas flow requirements for each ozone contactor (see below). 5.2 Initial Gas Flow Requirements It is assumed that normal operation will be to set the production scheme as Constant Concentration/Variable Gas Flow. With that in mind, the control system will initially calculate the required gas flow rate for each ozone contactor based on their individual ozone demands and the Initial ozone Concentration Setpoint, as entered by the operator: FDR = k x DCTa sPI Where FD, = Initial ozone contactor Gas Flow demands (in SCFM). CsP, = Initial ozone -in -gas Concentration set point as entered by the operator (in %/wt). Printed: 2023-10-11 Ozone System Control: Functional Design Specification . 9 of 29 k = unit dependent factor (— 0.8387) 5.2.1 Ozone Contactor Gas Flow Sizing Each ozone contactor can deliver ozone into the water via two (2) possible diffusing manifolds, located in the cell #1 and cell #3 respectively. Each manifold is equipped with a specific number of diffusers. Minimum (FCellMin) and maximum (FcellMax) flow rates for each diffuser must be respected to guarantee proper distribution within the cell, maximum transfer efficiency and minimum short-circuiting. The ozone system will dynamically calculate the minimum and maximum gas flow rates for each cell based on the following formula: Fcel1,All„ = FD;gmj„ X Diff FCeIIMa� = FDOlm X Di f Where Fwffmin = Minimum diffuser gas flow FD;flMax = Maximum diffuser gas flow Diff = Number of diffusers for a particular cell Contactor #1 Contactor #2 Cell1 Ce113 Cell1 Cell3 Number of Diffusers 32 32 32 32 Min Flow per diffuser (SUM) 0.3 0.3 0.3 0.3 Max Flow per diffuser (SCFM) 1.57 1.57 1.57 1.57 Quvo a, e udbeu un information available at the time this document was written. 5.2.2 Ozone Contactor Gas Flow Low Limit Minimum gas flow for a given ozone contactor (FCTMIN) is determined by the number of "active" manifolds and their respective minimum gas flow (as calculated above). When the ozone demand for a particular ozone contactor is low, the resulting gas flow demand might be below the value of FCTMIN. If this occurs, the efficiency of the ozone contactor may be reduced. When this occurs, the system will automatically lock the gas flow for that specific ozone contactor to FUMiN. FDA = FCTmiN The system will subsequently calculate an ozone -in -gas concentration set point as required by the ozone contactor to meet the lower level of ozone demand, while operating at a fixed gas flow (Constant Gas Flow/Variable Concentration). To determine the ozone contactor's ozone concentration requirements, the following formula is used. CSPCT.X = k X PDCT.i FCTMIN Where CsPcTx = ozone -in -gas Concentration as required by the specific ozone contactor, to meet the required ozone feed rate utilizing a minimum gas flow setting. k = unit dependent factor Printed: 2023-10-11 Ozone System Control: Functional Design Specification .10of29 The system will subsequently produce an alarm for the contactor with a message stating "Contactor X Low Flow". Since the system takes control of the production by locking the gas flow to its minimum and adjusting the concentration instead, the operator may not need to take any action. On the other hand, this alarm will at a minimum indicate to the the operator that a lower ozone production is being called for, and that reducing the number of "active" cells (or even contactors) is possible. It should be noted that decreasing the initial ozone concentration set point would increase the system's need for gas, which may correct the low limiting function. This way, the operator may not need to "de- activate" cells or shutdown contactors. 5.2.3 Ozone Contactor Gas Flow High Limit When the ozone demand for a particular ozone contactor increase, and the resulting gas flow demand rises above the value of FCTMax, the system will automatically lock the gas flow for that specific ozone contactor to FCTMAX• FDCTX — FcTA�tx The system will subsequently produce an alarm for the contactor with a message stating "Contactor X High Flow". Since this condition will run the risk of under -dosing, the operator should "activate" additional cells to accommodate the rise in gas flow, for a higher ozone demand. It should be noted that increasing the initial ozone concentration set point would lower the system's need for gas, which may correct the limiting function. This way, the operator may not need to "activate" more cells or turn -on contactors. 5.3 Ozone -in -gas Concentration Set point As a precursor to the actual ozone -in -gas concentration set point used, plant operation is required to provide the Initial ozone Concentration Set Point. This set point is manually entered and is limited to the ozone plant's allowed range of operation. With the Initial Concentration set point, and the resulting concentration requirements of all the ozone contactors in operation, the control system determines which of the Concentration set points it will utilize to satisfy the need in ozone demand. That is, by comparing all the results and the Initial Concentration set point, the lowest of the values will be used to then calculate the total plant gas flow requirements. FD = k x PD SPLI Where FD = Plant Gas Flow demands (in SCFM). CSPL1 = Lowest of all ozone -in -gas Concentration set points (in %/wt). k = unit dependent factor (— 0,8387) 5.3.1 Plant Gas Flow Low Limit As it is done for the individual ozone contactors, gas flow limits are also evaluated at a plant level, taking into consideration the minimum gas flow requirements of all other equipment in the plant (ozone generators, ozone destruct units, etc.). If the result of FD is determined to be below the minimum operating limits of any other equipment in the plant, FD, the system will automatically lock the plant required gas flow to FDMIN (the largest of all Equipment Minimum Gas Flow preset values). nnr.. 0121033-MP-010 Rev.2 Printed: 2023-10-11 Ozone System Control: Functional Design Specification . 11 of 29 FD = FDauN The system will subsequently calculate, once again, an ozone -in -gas concentration set point as required by the plant to meet the lower level of ozone demand, while operating at a fixed gas flow (Constant Gas Flow/Variable Concentration). To determine the plant's ozone concentration requirements, the following formula is used. PD CSP = k x FDMIN Where Csa = Actual ozone -in -gas Concentration. k= unit dependent factor 5.4 Final Gas Flow Requirements The actual ozone contactor's gas flow set point is now calculated using the following formula: FDCTa = FD x(�LDCTX P D Where FocTX = Actual Ozone Contactor Gas Flow Set Point (in SCFM) 5.5 Constant Gas Flow Mode vs. Variable Gas Flow Mode Although it is expected that the system will be operated primarily in Variable Gas Flow mode (where the system is left to decide how best to control both gas flow and ozone concentration), the entire plant will be forced to Constant Gas Flow mode only if the calculated gas flow demand is lower than the Plant Gas flow Low Limit. Gas flow limits, both low and high, will be controlled at the ozone contactor under all circumstances. File• ()191ng4&Aon-fnnnn I-, Panted 2023 10 11 Ozone System Control: Functional Design Specification p. 12 of 29 6 PERFORMANCES MONITORING 6.1 Ozone Generator Production P07-v = k x CoZx x FO, Where Cozx = Measured concentration at the generator discharge Fozx = Generator gas mass flow k = Unit dependent factor (- 1.1923) For each generator, the production is integrated and displayed. n.nk Qn VVFP Doc. Q121033-MP-010 Rev.2 Printed: 2023-10-11 Ozone System Control: Functional Design S ecification . 13 of 29 7 OZONE SYSTEM OPERATING SEQUENCE 7.1 Main commands The major commands to operate the ozone system include: • A manual Plant START -STOP command Any shutdown interlock (ambient -trip, global -trip or slow -trip interlocks) will shut down the plant. 7.2 Interlocks & Permissions 7.2.1 Generator Permissive Master permission(s): Release the control for the ozone generation. This permission is based on the following conditions: • Ozone Destruct Unit Running • Absence of either trip interlock This permission will source the "Start Enable" to the ozone generator control panels. 7.2.2 Generation Safety Under this category, one permissive and one interlock is produced. The "Production Enable" (permissive) allows power to the ozone generator, for ozone production. The "Power Limiter" (interlock) will limit the power to the ozone generator to 50%. The "Production Enable" is based on the following conditions: • Acceptable Dewpoint on the GOX header The "Power Limiter" is based on the following condition: • Nitrogen flow is below the required level (Low -Low) 7.2.3 Global -Trip Interlock (GTI) When this interlock turns ON the entire system shuts down immediately. The system cannot be switched ON while this interlock is active. This interlock is active when the following condition is detected: • Mushroom -type pushbutton (twist to release) are pressed • No ozone destruct unit is RUNNING, following a short delay, even though a plant -wide demand for destruction is set. 7.2.4 Ambient -Trip Interlock (ATI) When this interlock turns ON the entire system shuts down immediately, except for the ozone destructs. The system cannot be switched ON while this interlock is active. This interlock is related to the ambient leak monitoring by use of analytical devices located in strategic locations throughout the facility. In some circumstances and depending on where the monitoring instruments will be located, the ATI could affect only portions of the system, if segregation is possible. Under this interlock, the ozone destruct(s) will shut down once the post -destruct time has elapsed as if following the NORMAL shutdown sequence. File: Q121033MP010000.docx Printed 2023 10 11 Ozone System Control: Functional Design Specification p. 14 of 29 7.2.5 Slow -Trip Interlock (STI) This interlock groups the conditions to shutdown the ozone system under NORMAL shutdown sequence. The system cannot be switched back on while this interlock is active. This interlock is active when any one of these conditions is detected: • Liquid Oxygen (LOX) Sub -System Not Available • Vaporizer Sub -System Not Available • Gaseous Oxygen (GOX) Sub -System Not Available • Ozone Generator Sub -System Not Available • Ozone Contactor Sub -System Not Available How a sub -system is determined to being "Not Available" is defined further within the sub-system's descriptive paragraphs. 7.3 Sequence Status display The plant Sequence Status is displayed as: • STOPPED = ozone Generators Stopped • PURGING = ozone generator(s) flowing gas (pre or post purging). • RUNNING = At least one ozone generator is producing ozone (applying power to vessel) 7.4 Stan` -up Sequence The start-up sequence is permitted when the following is true: • No trip conditions exist. When the plant START command is selected, the sequence is as follows: • The LEAD and any other required ozone destruct (depending on total gas demand) is started • Once the system detects that the ozone destruct unit is running, the "START ENABLE" permissive to the ozone generator is given. • The LEAD and any other required ozone generator (depending on total ozone demand) will open their gas and cooling water valves, as a response to a start command. Unit(s) will purge through the ozone generator's purge line directly to the destruct unit(s). Whenever an ozone generator opens its cooling water valve(s), the system's cooling sub -system will operate and this, in accordance with the number of generators requiring cooling water. • The ozone generator(s) will purge for a minimum pre -determined time. Purge delay is dependent on minimum elapsed time, and adequate gas Dewpoint. Purge time may be extended beyond the pre -determined minimum period. Purging will continue as long as adequate Dewpoint levels are not met. • No additional commands are initiated, and no other operator intervention is needed. Once the previous conditions are satisfied (pre -purge period has ended and good dewpoint is reached), the system will immediately switch into ozone production by setting the PRODUCTION ENABLE interlock. Printed: 2023-10-11 Ozone System Control: Functional Design Specification n 15 of 29 • The operating ozone generator will open its ozone valve. Since gas flow through the plant is controlled at the contactors, the ozone system will react to the generator's ozone valve status, and control any ancillary equipment related to flowing gas (i.e.: Open the gas valves at the ozone contactors). • Nitrogen system, which would have been previously enabled either locally or remotely in manual or auto, will start controlling the flow to meet the desired set point. • Power to the ozone generator will ramp and continuously adjust to achieve and hold the desired ozone concentration. 7.5 Sequenced Shut -Down The sequenced shutdown is initiated by: • Detection of the SLOW -TRIP interlock • The removal of the ozone system demand, by selecting STOP The steps of the sequenced shutdown are: • The ozone production turns off, stopping power in the PSU(s). Disabling the ozone production disables the ozone concentration loop. Both a generator post -purge period and a PSU post -cooling period are initiated. The post -purge period is used for both purging the generator and any equipment downstream, through the ozone contactor, and for cooling the vessel. This requires that both gas and cooling water be flowing. • Once the post -purge delay is elapsed, all ozone generator valves (gas and cooling water) will close. o The "request for gas" will be removed, which will cause the "gas -related" ancillary equipment to shutdown. o The "request for cooling water" will remain until the PSU has completed its post -cooling. The PSU's post -cooling period is set slightly longer that the generator's post -purge period. • Once the PSU post -cooling delay is elapsed, the PSU cooling valve will close. o The "request for cooling water" will be removed, which will cause the "water -related" ancillary equipment to shutdown. • A post -destruct period is initiated to eliminate any remaining off -gassing ozone in the contactors. • Ozone destructs are turned off at the end of this delay. 7.6 Immediate Shutdown The immediate shutdown is caused by: • Detection of ambient -trip or global -trip In this case, no sequence is initiated. Instead, all the equipment is immediately ordered to either stop or close. The post -purge at the generator is eliminated and all units turn off instantaneously. During an ambient -trip situation, the ozone destruct unit(s) will retain their post -destruct time of operation. File: Q121033MP010000.docx nehL k %AICM Printed 2023 10 11 Ozone System Control: Functional Design Specification p. 16 of 29 8 LOX STORAGE SUB -SYSTEM Liquid oxygen is stored in two (2) permanent liquid oxygen storage tanks (T4007-1, T4007-2) Common to this sub -system (to both tanks), the principal instruments, devices and components are, but not limited to: • Remote Fill Station/LOX Truck Unloading Connection • Remote Fill Station Unloading Indicator Panel Per tank, the principal instruments, devices and components of this sub -system are, but not limited to: • Tank Pressure Relief Valve • Tank Pressure Indicator • Tank Pressure Transmitter Indicator • Tank Pressure Indicator • Tank Level Transmitter Indicator • Tank Manual Discharge Isolation Valve 8.1 Alarms with effects • LOX Tank #x Level Low Alarm (LAL); see "Subsystem Not Available" 8.2 Subsystem "Not Available" Alarms and conditions forcing the sub -system in "Not Available" state are: • Both Tank Levels are reporting Low Levels 8.3 Specific sub -system controls No specific or additional controls are configured or associated with this sub -system. Printed: 2023-10-11 Ozone System Control: Functional Design Specification .17of29 9 VAPORIZER SUB -SYSTEM Ozone is produced using gaseous oxygen (referred to as GOX) obtained by the evaporation of liquid oxygen (referred to as LOX). Liquid oxygen is evaporated using one of three (3) vaporizers. Per vaporizer, the principal instruments, devices and components of this sub -system are, but not limited to: • One (1) Ambient Vaporizer • One (1) Isolation Valve 9.1 Alarms with effects • Vaporizer #x Isolation Valve Discordance Alarm (Failure to OPEN): Forces isolation valve to OFFLINE mode 9.2 Subsystem "Not Available" Alarms and conditions forcing the sub -system in "Not Available" state are: • All Vaporizer Isolation Valves are OFFLINE mode 9.3 Specific sub -system controls 9.3.1 Priority Selection, Rotation and Demand Although the vaporizer's isolation valve can be selected to operate in MANUAL, an AUTO ROTATION sequence is available. The AUTO ROTATION uses a retentive timer monitoring the number of hours a specific vaporizer is running (isolation valve OPEN). When the accumulated running time equals the operator -entered time setting, the DUTY, STANDBY and DEFROST vaporizers will interchange their state automatically, causing the now -DEFROST vaporizer isolation valve to close, and the now -DUTY vaporizer isolation valve to open. In addition, the operator can manually force a rotation by changing the DUTY/STANDBY/DEFROST priority selection of the vaporizer valves. The AUTO ROTATION timer will reset when this occurs. During any priority change, manual or automatic, an overlap period will be respected. During this overlap period, both the now -DEFROST and now -DUTY vaporizer valves will be opened at the same time, as determined by an operator setting, to avoid gas flow interruption in the system. Whether the AUTO ROTATION mode is enabled or not, if ever the DUTY vaporizer isolation valve is set to OFFLINE mode (manually by the operator or automatically by the control system), the STANDBY vaporizer isolation valve will be forced to open, providing that the STANDBY vaporizer isolation valve is in AUTO. Similarly and under those conditions, if the STANDBY vaporizer isolation valve is called to operate but is itself in OFFLINE mode, the DEFROST vaporizer valve will be called into operation. Printed 2023 1011 Ozone System Control: Functional Design Specification p. 18 of 29 10 OXYGEN FEED GAS MONITORING AND CONTROL The vaporizers will discharge into a common header, also called the GOX header. The principal instruments, devices and components of this sub -system are, but not limited to: • Paralleling Trim Heater Lines, each equipped with: ■ One (1) Trim Heater ■ One (1) Low Temperature Shutdown Valve • Common Header ■ One (1) Temperature Transmitter Indicator ■ One (1) Temperature Low Switch Paralleling GOX Feed Lines, each equipped with: ■ One (1) Differential Pressure Indicator ■ One (1) Pressure Transmitter Indicator ■ One (1) Emergency Automatic Shutdown Isolation Valve ■ First Cross -over pipe ■ One (1) Particulate Filter equipped with a Differential Pressure Indicator ■ Second Cross -over pipe ■ One (1) Pressure Reducing/Regulating Valve ■ Third Cross -over pipe ■ One (1) Pre -Nitrogen Dew Point Transmitter Indicator ■ One (1) Temperature Transmitter Indicator ■ Nitrogen Injection Point ■ One (1) Post -Nitrogen Dew Point Transmitter Indicator ■ One (1) Flow Transmitter Indicator ■ Forth cross -over pipe w/ One (1) Differential Pressure Indicator 10.1 Alarms with effects • Pre -Nitrogen ■ GOX Dewpoint High Alarm (AAH): While the ozone system is starting up, will not permit power on the generator vessel. Part of the "Production Enable" interlock. ■ GOX Dewpoint High -High Alarm (AAHH): Monitored only when ozone is being produced; shuts down the ozone system. • Post -Nitrogen ■ GOX Dewpoint High Alarm (AAH): While the ozone system is starting up, will not permit power on the generator vessel. Part of the "Production Enable" interlock. File: Q121033MP010000.docx Oshkosh WFP Doc. Q121033-MP-010 Rev.2 Printed: 2023-10-11 Ozone System Control: Functional Design Specification . 19 of 29 ■ GOX Dewpoint High -High Alarm (AAHH): Monitored only when ozone is being produced; shuts down the ozone system. 10.2 Subsystem "Not Available" Alarms and conditions forcing the sub -system in "Not Available" state are: ■ Pre -Filter GOX Dewpoint High -High Alarm (AAHH) ■ Post -Filter GOX Dewpoint High -High Alarm (AAHH) 10.3 Specific sub -system controls ■ None File: Q1210331VIP010000.docx Oshkosh WFP Doc. Q121033-MP-010 Rev.2 Printed 2023 1011 Ozone System Control: Functional Design Specification p. 20 of 29 11 NITROGEN SYSTEM To improve the efficiency of the ozone generators, a small amount of nitrogen must be added to the oxygen, upstream of the ozone generators. Obtaining the required nitrogen is as simple as compressing and drying atmospheric air. The principal instruments, devices and components of this sub -system are, but not limited to: Two (2) Air Compressor, each equipped with an upstream air -filters • A single Air Receiver Tank equipped with... ■ A Pressure Relief Valve ■ Three (3) Pressure Switches (PSL, PSLL, PSH) ■ An Auto -Drain Valve Paralleling filter/dryer lines, each equipped with... ■ One (1) Coalescing Filter ■ One (1) Desiccant Dryer ■ One (1) Particulate Filter One (1) Pressure Regulating/Reducing Valve One (1) Pressure Transmitter Indicator One (1) Combination Flow Control/Flow Transmitter Device ■ Paralleled with one (1) Flow Indicator 11.1 Alarms with effects Nitrogen Flow Low -Low (FALL): Will limit power applied to any running ozone generator. Part of the "Power Limiter" interlock. 11.2 Subsystem "Not Available" Alarms and conditions forcing the sub -system in "Not Available" state are: Nitrogen Generator General FAULT 11.3 Specific sub -system controls A nitrogen -to -oxygen ratio set point is entered by the operator. The control system will apply this setting to the TOTAL GAS FLOW required value (calculated by the system), and the resulting required nitrogen flow value will be sent directly to the skid mounted flow controller. There, the controller will take care of maintaining the desired nitrogen flow. This is true whenever the selector associated for nitrogen control is set to CALCULATED mode. The set point mode can also be set to OPERATOR mode. In this mode, the operator will enter the desired nitrogen flow, in the correct units. The control system will always cap the set point (CALCULATED or OPERATOR) so to maintain adequate flow through the system. No matter the mode selected, LOW and LOW -LOW nitrogen flow alarms are enabled. n�, 0121033-MP-010 Rev.2 Printed: 2023-10-11 Ozone System Control: Functional Design Specification . 21 of 29 12 OZONE GENERATION SUB -SYSTEM Ozone (03) is a tri-atomic gas, obtained by the ionization of oxygen (02). It is an extremely strong oxidizing agent but is unstable and spontaneously degrades back into oxygen. As a consequence, it cannot be stored and must be produced on site just prior to use. Ozone is produced by means of a high -voltage AC current applied between two electrodes separated by a gap through which oxygen flows. One of the electrodes is covered with a ceramic dielectric. Gaseous oxygen is fed to three (3) ozone generators working in a LEAD/LAG1/LAG2 mode. Each ozone generator is provided as a package and is viewed by the control system as such. The principal instruments, devices and components of each package are, but not limited to: • An Ozone Generator Vessel • An Oxygen Feed Gas Line equipped with: In One (1) Automatic Isolation Valve ■ One (1) Flow Transmitter Indicator ■ One (1) Pressure Transmitter Indicator ■ One (1) Temperature Transmitter Indicator • One (1) Pressure High Switch ■ One (1) Pressure Low Switch ■ One (1) Pressure Relief Valve • An Ozone Discharge Gas Line equipped with: ■ One (1) Temperature Transmitter Indicator ■ One (1) Temperature High Switch ■ One (1) Automatic Isolation Valve ■ One (1) Ozone Concentration Transmitter Indicator • An Ozone Purge (to destruct) Gas Line equipped with: ■ One (1) Automatic Isolation Valve ■ One (1) Orifice Plate • A CW Supply Line equipped with: ■ One (1) Automaic Isolation Valve ■ One (1) Temperature Transmitter Indicator • One (1) Pressure Relief Valve • A CW Return Line equipped with: ■ One (1) Air Relief Valve ■ One (1) Temperature Transmitter Indicator Printed: 2023 10 11 Ozone System Control: Functional Design Specification p. 22 of 29 ■ One (1) Temperature High Switch ■ One (1) Flow Transmitter Indicator • A Power Supply Unit (PSU) • A PSU CW Supply Line • A PSU CW Return Line equipped with: ■ One (1) Temperature Transmitter Indicator • One (1) Flow Indicator 12.1 Alarms with effects • Ozone Generator General Fault: Will force the specific generator's control mode to OFFLINE mode. 12.2 Subsystem "Not Available" Alarms and conditions forcing the sub -system in "Not Available" state are: • All Ozone Generator packages are OFFLINE 12.3 Specific sub -system controls Each ozone generator package is provided with its own local control panel equipped with a PLC and an OIT. The local control panel contains all required hardware and software components and is connected to all the instruments on the ozone generator to safely operate the generator. The generator may be operated either from the local panel or from the ozone plant central control system. For complete detail, please refer to the "Ozone Generator Control Panel - Operations Manual". 12.3.1 Priority Selection, Rotation and Demand The remote operation is allowed only when the LOR selection at local OIT is selected in REMOTE. Two remote modes are available; if the generator is in AUTO, the ozone generator is started and stopped from the Main sequence in relation with the ozone demand and the priority selection. If the generator is in MANUAL, it must be started and stopped from its individual START -STOP commands. When more than one ozone generator is running, each ozone generator receives the same gas flow and the same ozone -in -gas concentration set point. The MOCP is programmed with the generator's production characteristic with respect to the ozone concentration. When the ozone demand increases and the ozone generator in operation reaches 95% (entered by the operator) of its rated production capacity, the LAG generator is started. The total gas flow is adjusted while the second unit is in start-up (or shutdown) to assure that production is not affected. In opposite, if the ozone demand drops and two generators are running below 65% (entered by the operator) of their rated production capacity, the LAG generator is stopped. When a shutdown alarm is generated by the local panel (PSU), the MOCP receives the GENERATOR FAULT signal, which switches off the generator. If the standby generator is in AUTO and is available (no faults), it is immediately started. To avoid interrupting the gas flow, the gas flow is maintained on the failed generator until the standby generator has started (only with faults caused by a slow -trip interlocks). Printed: 2023-10-11 Ozone System Control: Functional Design Specification p 23 of 29 13 COOLING WATER SUB -SYSTEM Generating ozone causes huge amounts of heat to be generated. The method used to remove/transport the heat generated by both the vessels and the PSU's is to flow cooling water through the mentioned equipment. Two (2) cooling water packages are provided, an OPEN -LOOP and a CLOSED -LOOP system. At the center of the Cooling Water System are: • Three (3) Water -to -Water Plate Heat Exchangers The principal instruments, devices and components of the Open -Loop CW system are, but not limited to • Common Header Upstream of the Heat Exchangers / Open -Loop CW Supply ■ Three (3) Open -Loop Cooling Water Supply Pumps • Individual Heat Exchanger / Open -Loop CW Supply (typical of three) ■ One (1) Flow Transmitter Indicator ■ One (1) Automatic Isolation Valve ■ One (1) Pressure Transmitter Indicator • Individual Heat Exchanger / Open -Loop CW Return (typical of three) ■ One (1) Air -Relief Valve • Common to Heat Exchanger / Open -Loop CW Supply & Return (typical of three) ■ One (1) Differential Pressure Transmitter Indicator The principal instruments, devices and components of the Closed -Loop CW system are, but not limited to • Common Header Upstream of the Heat Exchangers / Closed -Loop CW Return from Generators ■ One (1) Air Separator ■ One (1) Chemical Pot Feeder ■ One (1) Expansion Tank • Individual Heat Exchanger / Closed -Loop CW Return from Generators (typical of three) ■ One (1) Automatic Isolation Valve ■ One (1) Closed -Loop Cooling Water Pump ■ One (1) Pressure Transmitter Indicator • Individual Heat Exchanger / Closed -Loop CW Supply to Generators (typical of three) ■ One (1) Air -Relief Valve • Common to Heat Exchanger / Closed -Loop CW Return to & Supply to Generators (typical of three) ■ One (1) Differential Pressure Transmitter Indicator Printed: 2023 10 11 Ozone System Control: Functional Design Specification p. 24 of 29 13.1 Alarms with effects • Open -Loop CW Pump General Fault: Will force the specific pump's control mode to OFFLINE mode • Closed -Loop CW Pump General Fault: Will force the specific pump's control mode to OFFLINE mode • Closed -Loop CW Pump Discharge Pressure High -High: Will force the specific pump's control mode to OFFLINE mode 13.2 Subsystem "Not Available" Alarms and conditions forcing the sub -system in "Not Available" state are: • All three Open -Loop CW Pumps are OFFLINE • All three Closed -Loop CW Pumps are OFFLINE 13.3 Specific sub -system controls 13.3.1 Priority Selection, Rotation and Demand Typical for either the Open -Loop or Closed -Loop cooling water sub -systems, the individual pumps may be controlled in LOCAL/MANUAL, via the interfacing provided at the Motor Control Center (MCC). Equipped with a LOCAL -OFF -REMOTE (LOR) or LOCAL -REMOTE (LR) selector, when in LOCAL, a pump can be started at the MCC. Light indicators on the MCC will show pump RUNNING and FAULT status (assumed). When the local selector (LOR or LR) is placed in REMOTE, control is by MOCP. For each pump, the operator will be able to select either AUTO or MANUAL control. When selected in MANUAL, the operator can start and stop the pump. For the Open -Loop Supply Pumps, when selected in AUTO, the pumps will start and stop based on the number of ozone generators requiring cooling water. For every generator, one closed -loop pump will operate and this, based on their assigned LEAD/LAG1/LAG2 state as selected by the operator. If the priority is changed while the system is in operation, an overlap time is respected, where both pumps will operate simultaneously so to maintain water flow to the Open -Loop circuit. For the Closed -Loop Pumps, when selected in AUTO, the pumps will start and stop based on the number of ozone generators requiring cooling water. For every generator, one closed -loop pump will operate and this, based on their assigned LEAD/LAG1/LAG2 state as selected by the operator. Operation of any one pump will trigger the opening of the corresponding Open -Loop Automatic Isolation valve associated to the Heat Exchanger to which the Open -Loop pump is connected to. If the priority is changed while the system is in operation, an overlap time is respected, where both pumps will operate simultaneously so to maintain water flow to any operating Ozone Generator. Printed: 2023-10-11 Ozone System Control: Functional Design Specification p 25 of 29 14 OZONE CONTACTOR SUB -SYSTEM There are two (2) Ozone Contactors and each one will be fed by its own Ozone gas line, originating from the common header discharge downstream of the ozone generators. The principal instruments, devices and components of each contactor are, but not limited to • A Main Ozone Feed Gas Line, equipped with: ■ One (1) Flow Transmitter Indicator • One (1) Automatic Modulating Valve ■ One (1) Pressure Transmitter Indicator ■ One (1) Temperature Transmitter Indicator • The first of two Diffuser Manifold Feed Gas lines, equipped with: ■ One (1) Flow Transmitter Indicator ■ One (1) Automatic Modulating Valve ■ One (1) Pressure Transmitter Indicator ■ Thirty-two (32) diffuser stones • The second of two Diffuser Manifold Feed Gas lines, equipped with: ■ One (1) Flow Transmitter Indicator ■ One (1) Automatic Modulating Valve ■ One (1) Pressure Transmitter Indicator ■ Thirty-two (32) diffuser stones • One (1) Pressure Relief/Vacuum Breaker Valve (mounted on roof of contactor) • An Off -Gas Discharge Line, equipped with: ■ One (1) Pressure/Vacuum Transmitter Indicator ■ One (1) Demister with a Differential Pressure Transmitter Indicator ■ One (1) Pressure Relief/Vacuum Breaker Valve ■ One (1) Medium Ozone Concentration Analyzer Transmitter Indicator • Nine (9) Sample points • Five (5) Dissolved Ozone Monitoring Transmitter Indicators, each having their own sample pump 14.1 Alarms with effects • None 14.2 Subsystem "Not Available" Alarms and conditions forcing the sub -system in "Not Available" state are: Panted 2023 10 11 Ozone System Control: Functional Design Specification p. 26 of 29 Both Contactors are set to OFFLINE mode 14.3 Specific sub -system controls 14.3.1 ONLINE/OFFLINE State Each contactor is set in ONLINE and OFFLINE state by the operator. This state will not change by itself. It is determined by the operator. When a contactor is ONLINE, it indicates that water is flowing, and that ozone dosage is desired. Ultimately, this is an operational decision. The required ozone production for each individual ozone contactor is calculated by means of the individual raw water flow (be it measure, calculated or manual entered by the operator) and the individual ozone dosage set point. nor.. 0121033-MP-010 Rev.2 Printed: 2023-10-11 Ozone System Control: Functional Design Specification . 27 of 29 15 OZONE DESTRUCT SUB -SYSTEM An operating ozone contactor will release almost all the gas being introduced. A small amount of ozone is trapped with that volume of gas. An ozone destruct unit will provide two services. The first is to pull the gas out of the contactors and maintain a slight vacuum within the contactor headspace and off -gas piping by means of a vacuum blower. This will avoid pressurisation of the contacting structures and avoid unwanted release of medium concentrations of ozone into the surrounding areas. The second service is to neutralize/destroy any of the ozone carried over in the off -gas stream, by means of a catalyst bed. Although a demister is installed on the off -gas line (sized for maximum efficiency), the gas may contain a small amount of water in vapor form. The catalyst, being very sensitive to liquid water, is protected from the potentially "wet" gas by means of an electric heater placed upstream of the catalyst bed. The heater will evaporate any trace of liquid water and drop the gas Dewpoint so to make the gas adequate to flow through the catalyst bed, with minimal chance of contamination. A temperature controller (TIC) installed on the individual units' local control panel controls the power to the heating element. The sub -system is made-up of three (3) ozone destructs working in a LEAD/LAG mode. Each ozone destruct is provided as a package and is viewed by the control system as such. The principal instruments, devices and components of each package are, but not limited to: • An Off -Gas Line equipped with: ■ One (1) Automatic Isolation Valve ■ Air Intake Line, equipped with: • One (1) Orifice Plate ■ One (1) Automatic Isolation Valve ■ One (1) Air Intake Filter ■ One (1) Pre -Heater Temperature Transmitter Indicator ■ One (1) Pre -Heater ■ One (1) Pre -Heater Temperature Element/Probe • A Heated Gas Line equipped with: ■ One (1) Temperature Transmitter Indicator ■ One (1) Catalyst Bed equipped with a Differential Pressure Transmitter Indicator • A Vent -Gas Line equipped with: ■ One (1) Temperature Transmitter Indicator ■ One (1) Vent -Gas Ozone Concentration Transmitter Indicator ■ One (1) Vacuum Blower equipped with a Differential Pressure Transmitter Indicator ■ One (1) Silencer • One (1) Local Control Panel 0 One (1) Power Panel Printed 2023 10 11 Ozone System Control: Functional Design Specification p. 28 of 29 15.1 Alarms with effects Vent -Gas Concentration HIGH Alarm (AAH): The "next" Ozone Destruct Units will be called to operate Vent -Gas Concentration HIGH -HIGH Alarm (AAHH): Condition to the Ambient -Trip Interlock (ATI) Ozone Destruct General Fault: Will force the specific destruct's control mode to OFFLINE mode. 15.2 Subsystem "Not Available" Alarms and conditions forcing the sub -system in "Not Available" state are: All three Ozone Destruct packages are OFFLINE 15.3 Specific sub -system controls Each ozone destruct package is provided with its own local control panel. The local control panel contains all required hardware components and is connected to all the instruments on the ozone destruct skid to safely operate the destruct unit. The destruct unit may be operated either from the local panel or from the ozone control system. For complete detail, please refer to the "Ozone Destruct Control Panel - Operations Manual". 15.3.1 Priority Selection, Rotation and Demand The remote operation is allowed only when the LOR selection at the local panel is selected in REMOTE. Two remote modes are available; if the destruct is in AUTO, the ozone destruct is started and stopped from the main sequence in relation with the ozone plant demand and the priority selection. If the destruct is in MANUAL, it must be started and stopped from its individual START -STOP commands. When a shutdown alarm is generated by the local panel, the MOCP receives the DESTRUCT FAULT signal, which switches off the destruct. If the standby destruct is in AUTO and is available (no faults), it is immediately started. Printed: 2023-10-11 Ozone System Control: Functional Design Specification n 29 of 29 16 AMBIENT GAS DETECTION AND EMERGENCY SHUTDOWN SUB -SYSTEM The Ambient Gas Detection and Emergency Shutdown system is not a single component, but is made-up of many instruments, connected to the two (2) localised alarm panels, strategically located as well as to the MOCP panel via hardwired link and affects the two out of the three major plant -level interlocks. The principal instruments, devices and components associated with the Ambient Gas Detection system are: • In the ozone generation room/area ■ Two (2) Ambient Oxygen Concentration Transmitter Indicator ■ Two (2) Ambient Ozone Concentration Transmitter Indicators • In the gallery area • Five (5) Ambient Oxygen Concentration Transmitter Indicator ■ Two (2) Ambient Ozone Concentration Transmitter Indicators The principal instruments, devices and components associated with the Emergency Shutdown system are: • In the ozone generation room/area ■ Ozone Generator Room Alarm Panel equipped with Emergency Stop Pushbutton ■ Four (4) Field Emergency Stop Pushbuttons ■ A series of strobes and horns • In the gallery area ■ Gallery Area Alarm Panel equipped with Emergency Stop Pushbutton ■ Three (3) Emergency Stop Pushbuttons ■ A series of strobes and horns • One the MOCP ■ One (1) Emergency Stop Pushbuttons 16.1 Alarms with effects • (Typical) Ambient Ozone Concentration HIGH -HIGH Alarm (AAHH): Condition to the Ambient -Trip Interlock (ATI) • Ambient Oxygen Concentration HIGH -HIGH Alarm (AAHH): Condition to the Ambient -Trip Interlock (ATI) • Any Emergency Stop ACTIVE: Condition to the Global -Trip Interlock (GTI) 16.2 Subsystem "Not Available" This sub -system does not generate a "NOT AVAILABLE" status. 16.3 Specific sub -system controls Both the Ozone Generator Room and the Gallery Area Alarm Panel will act as the interface between the MOCP and the facility ventilation systems. Both Alarm Panels will also generate hardwired interlock to key equipment, such as the ozone generators and the oxygen shutoff valves, providing a first order shutdown to critical equipment. October 12, 2023 Anticipated fluctuation in electrical power, including peak draws during startup, is a critical consideration for many electrical systems. During startup, certain electrical devices or equipment may require a higher initial current to overcome inertia or to establish their operational state. This surge in power demand can lead to temporary voltage drops or instability in the electrical grid. To address these fluctuations and ensure the reliability of the electrical supply, various measures can be taken, such as: 1. Soft Starters: Implementing soft starters for motors and equipment can reduce the initial power surge during startup, thus minimizing the impact on the electrical system. 2. Advanced Grid Management: Utilizing smart grid technologies, predictive analytics, and demand response programs can help manage and balance power fluctuations more effectively. 3. Emergency Generators: Having backup generators in place ensures a stable power supply during peak draws and unexpected outages. 4. Power Quality Monitoring: Continuous monitoring and analysis of power quality can help identify and address fluctuations in real-time. 5. Regulatory Compliance: Ensuring compliance with industry standards and regulations is essential to mitigate power quality issues. It is crucial to anticipate and plan for these fluctuations to maintain a reliable and stable power supply, especially in situations where sudden and significant draws during startup can impact operational efficiency and safety. With that in mind, when considering the ozone system at this facility, and the equipment that will be installed and used for the purpose of producing and delivering ozone, Veolia believes that there is little reason for concern. The Ozone Generators and associated Power Supply Units are the main power draws as far as the ozone system is concerned. The Power Supply Unit are designed and tuned such that sudden changes in ozone demands do not result in sudden changes in power demands. This is achieved simply and efficiently by tuning the Power Supply's power controller with the appropriate ramp times and factors. This behavior is similar to having a Variable Speed Drive (VFD) on a large pump/motor, and configuring it locally, such that it ignores external inappropriate rapid changes in operation. The same can be said about the Ozone Destruct Units, where a VFD is actually used to control the Vent Blower's speed. It is locally configured so to avoid sudden increases in power demands. Veolia Water Technologies Treatment Solutions USA, Inc.. Anticipated Fluctuation. Docx 600 Willow Tree Road, Leonia, NJ 07605 All other equipment, such as the Cooling Water Pumps, open -loop and closed -loop alike, or the compressors on the Nitrogen Boost System, are much too small and will draw very little power in relation to the main feeder. Their affect on the main incoming power will be insignificant and may not even be noticeable even when utilizing "Advanced Grid Management" software or "Power Quality Monitors". Anticipated Fluctuation.Docx Page 2 of 2 x G w xx x - x � m N •, � � H � N � « a 9 +s3 w�x a 3 0 u� �F uLL.. E u�uw EuE 3L. 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I IY I O ,t-I To et -I Z Z O O O O N O d O d g N ? o W 0 0 0 ud u O� OO2OOo October 12, 2023 Subject: City of Oshkosh Water Filtration Plant Ozone System Package Purchase City of Oshkosh, WI Project No. 8679292 G. Bid Supplement 1 — 2.5.2—Table of Site Times In accordance with Specification Section 44 44 56.11 — Sellers Special Services, Veolia shall be providing the following Technical Support and Services: L. Services — Installation Supervision, Commissioning, Testing and Training Veolia shall provide the following commissioning, testing, and training services in accordance with par. 3.02 of specification section 13290 including the following: 1. Phase 1: Inspection and Commissioning • Ten (10) person -days for installation assistance, inspection, checkout and pre - commissioning of 03 Gen/PSU, Ozone Destruct, CW System, MOCP, Analyzers and Nitrogen Boost system • Twenty (20) person -days for functional and Operational Readiness Testing for 03 Generation system equipment that is part of phase 1 • Five (5) person -days for LOX-GOX System installation assistance, inspection and checkout of Manufacturer Proper Installation • Five (5) person -days for functional and operation readiness testing for the LOX-GOX System • Five (5) person -days for Ozone Dissolution System installation assistance, inspection and checkout of Manufacturer Proper Installation • Five (5) person -days for functional and operation readiness testing for the Ozone Dissolution System 2. Phase 2: Inspection and Commissioning • Five (5) person -days for installation assistance, inspection, checkout and pre - commissioning of 03 Gen/PSU, Ozone Destruct, CW pumps, and final MOCP integration • Ten (10) person -days for functional and Operational Readiness Testing for 03 Generation system equipment that is part of phase 2Performance Testing • One (1) trip of five (5) days on site for equipment performance testing SUEZ Treatment Solutions, Inc. Table Of Site Times_FINAL.Docx 600 Willow Tree Road, Leonia, NJ 07605 3. System Performance Demonstration Veolia shall perform the System Performance Demonstration testing in accordance with par. 3.03.E of section 44 44 56.11. 4. Operational Availability Demonstration (OAD): At the completion of the System Performance Testing a seven (7) day continuous test shall be run without significant interruption 5. Training Veolia shall provide the required Training as part of Phase 1 and Phase 2 as detailed in par. 3.04 of specification section 44 44 56.11 Note: Additional services if requested due to no fault of Veolia, are available at the rate of $1460 per day plus travel and living expenses Table Of Site TimeS_FINAL.Dou Page 2 of 2