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PEM ElectrolyzerHylyzer Hydrogen Generator
Hylyzer Hydrogen Generator Installation, Operation and Maintenance Manual
Revision 3This product is protected under one or more of the following US Patents: 7,117,106 and/or other pending patents.
DOC. P/N: 1039133-03
We're Ready.
PEM ElectrolyzerHylyzer Hydrogen Generator
Hylyzer Hydrogen Generator Installation, Operation and Maintenance ManualRevision 3
All rights reserved. No part of this manual may be reproduced or transmitted in any form or by any means, electronic or mechanical, including photocopying, or recording, without written permission from Hydrogenics Corporation.
Printed in July 2011.
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PEM ELECTROLYZER
Revision History
Warranties and LiabilitiesGuarantees, warranties, and liability limitations are described in the contractual agreements between Hydrogenics Corporation and the buyer.
The information included in this manual has been reviewed for accuracy and completeness but Hydro-genics Corporation reserves the right to revise the included information at any time, without notice.
Patents, Trademarks and Proprietary RightsThis product is covered under the following US patents: 7,117,106 and/or other pending patents. Other brand or product names are patented trademarks or registered trademarks of their respective owners.
Hydrogenics, HyPM, HyPX, HySTAT, HyLYZER, HyWARE are trademarks of Hydrogenics Corporation. “Hydrogenics” is a registered trademark of Hydrogenics Corporation in Canada, USA, Europe and Japan. HyPM and HyWARE are registered trademarks of Hydrogenics Corporation in Canada, USA and Europe. Other brand or product names marked ® are the registered trademarks of their respective owners.
The information, data, and illustrations contained in this manual are the property of Hydrogenics Corpo-ration and may not be reproduced or transmitted in any form or by any means, electronic or mechanical, without the prior written permission of Hydrogenics Corporation.
About Hydrogenics CorporationHydrogenics Corporation is a leading global developer of clean energy solutions, advancing the Hydro-gen Economy by commercializing hydrogen and fuel cell products. The company has a portfolio of prod-ucts and capabilities to serve the hydrogen and energy markets of today and tomorrow.
1 | IntroductionThis is the Installation, Operation and Maintenance manual for the Hydrogenics Hylyzer Hydrogen Generator, part number 1039008.
1.1 Intended AudienceThis manual is intended as the primary technical reference for users of Hydrogenics’ Charge Station product.
Hydrogenics assumes that appropriate end-user documentation will be prepared by the systems integrator for use by its customers. The integration information required for installing, setting up, controlling and maintaining the Charge Station is presented in this manual.
1.1.1 Technical Terms and AbbreviationsFor definition of the potentially unfamiliar terms and abbreviations used in this man-ual, refer to Appendix A:“Glossary” on p. 1.
Some terms that do not appear in the manual have been included to help gain a gen-eral understanding of Hydrogenics’ electrolyzer technology.
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INTENDED USE OF THE PRODUCT PEM ELECTROLYZER
The terms “user” or “operator” in this manual refer to the party who will oversee the Charge Station’s (automatic) operation. In most cases, the direct “operator” will be a system control device, which must be programmed to respond to the Charge Station’s fault messages and other feedback safely and appropriately for the intended applica-tion.
1.2 Intended Use of the ProductThe Hylyzer Hydrogen Generator uses clean de-ionized water and electricity to produce hydrogen and oxygen.
1.3 Customer AssistanceFor technical assistance with the installation, operation or maintenance of this product contact:
1.4 Reference DocumentsA list of recognized guidelines applicable to hydrogen installations, fuel cells and related systems and technologies is presented here for reference. Anyone responsible for such an installation or fuel cell application should become familiar with the applica-ble regulations of their local authorities.
1.4.1 Compressed Gas Association (CGA) PublicationsCompressed Gas Association Inc.4221 Walney Road, 5th FloorChantilly, VA 20151Phone: 703-788-2700Fax: 703-961-1831www.cganet.com
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL REFERENCE DOCUMENTS
G-5 Hydrogen Physical Properties
G-5.3 Commodity Specifications for Hydrogen
G-5.4 Standard for Hydrogen Piping at Consumer Locations
G-5.5 Hydrogen Vent Systems
S-1.2 Pressure Relief Device Standards-Part 2 - Cargo and Portable Tanks for Com-pressed Gases
1.4.2 National Fire Protection (NFPA) Association PublicationsNational Fire Protection Association1 Batterymarch Park,PO Box 9101,Quincy, MA 02269-9101, USAPhone: 617-770-3000Fax: 617-770-0700www.nfpa.org
NFPA 1 Uniform Fire Code
NFPA 55 Standard for the Storage, Use, and Handling of Compressed Gases and Cryo-genic Fluids in Portable and Stationary Containers, Cylinders, and Tanks.
NFPA 70 National Electric Code
1.4.3 The Society of Automotive Engineers (SAE)SAE International400 Commonwealth DriveWarrendale, PA 15096-0001Phone: 1-877-606-7323Fax: 724-774-0790www.sae.org
SAE J2578 Recommended Practice for General Fuel Cell Vehicle Safety
1.4.4 International Organization for Standardization (ISO)International Organization for Standardization (ISO)1, ch. de la Voie-CreuseCase postale 56
ISO 22734-1:2008 - Hydrogen generators using water electrolysis process -- Part 1: Industrial and commercial applications
1.4.5 International Organization for Standardization (ISO)Bureau de Normalisation du Quebec333, rue FranquetQuébec, QC G1P 4C7Phone: 1-418-652-2238Fax: 1-418-652-2292www.bnq.qc.ca
1784-000 CAN/BNQ - Canadian Hydrogen Installation Code
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2 | SafetyInstallations and equipment supplied by Hydrogenics are designed to comply with relevant safety standards and to prevent the formation of flammable atmospheres. The equipment and protective systems are designed and manufactured to ensure safe operation.
The systems and equipment shall be operated and maintained by qualified and authorized personnel only. Read this manual thoroughly before proceeding. Retain this manual for future reference.
Personnel responsible for operating or maintaining the equipment described in this manual must:
Read, understand and comply with the instructions presented throughout this manual;
Read the “Safety Information” section of this manual in order to understand the potential hazards associated with the systems or equipment.
Retain this manual for future reference.
Fully understand and comply with all applicable local safety by-laws, codes, and regulations.
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WARNING LABELS AND SYMBOLS PEM ELECTROLYZER
2.1 Warning Labels and SymbolsBe aware of the warning and cautionary signs, labels, and faults associated with the equipment and the area where you are working. These symbols, as well as the notices in this publication marked as Warning, Caution and Note, should be observed to ensure your own personal safety, as well as the safety of others, and to protect the product and its components from damage.
When working with the Charge Station, adhere to any warning and cautionary symbols that may be attached to the components. For more information on these symbols, refer to the Workplace Hazardous Material Information System (WHMIS) handbook.
2.1.1 Typical Hazard SymbolsMake sure you are familiar with all safety or hazard symbols in use in your workplace. The following list is not exhaustive, but does represent typical potential hazards which may be associated with the product in some operating environments:
CAUTION: Refer to Accompanying DocumentsThis symbol indicates important instructions accompanying the product or, used within a document, indicates potential hazards of a general nature.
WARNING: Electrical HazardThis symbol indicates the potential for high voltages within the product that may present a risk of electric shock.
WARNING: Hot SurfaceThis symbol indicates that the product may be hot enough in some areas to cause burns to the skin if touched.
WARNING: FlammableThis symbol indicates that the product may cause a fire or an explosion when exposed to heat, sparks, or flames or as a result of friction.
WARNING: Explosive or Flammable Gas AtmosphereThis symbol indicates that the product may cause a flammable gas atmosphere that may explode when exposed to heat, sparks, flames, or as a result of friction.
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL WARNING LABELS AND SYMBOLS
WARNING: Oxygen Enrichment (Toxic Atmosphere/Inhalation)This symbol indicates that the product may pose a risk of oxygen enrichment if not properly ventilated.
WARNING: High Gas PressureThis symbol indicates that the product develops gas pressures that may cause injury if released suddenly.
CAUTION: Protective Conductor Terminal (Ground)This symbol identifies a location for grounding equipment to Protective Earth (P.E.). As a warning, it also indicates that grounding is required for safe operation of the equipment.
2.1.2 Safety Notices in the ManualSeveral conventions and symbols are used throughout this manual to ensure the safe and proper operation of the equipment. The integrator(s) should carefully read and fully understand the information these conventions and symbols provide:
NOTE: Notes provide supplementary detail such as exception conditions, alternative methods for a task, time-saving tips, and references to related information.
The words Warning and Caution are used to draw attention to potential hazards of differing levels of severity. Each such hazard notice identifies a specific risk, lists the potential consequences, and indicates the action required to avoid or remedy the risk:
WARNING: These notices describe precautions to prevent hazardous conditions that may cause injury or death to people working with the equipment.
CAUTION: These notices describe precautions to prevent hazardous conditions that may dam-age the equipment.
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POTENTIAL HAZARDS AND SAFETY PRECAUTIONS PEM ELECTROLYZER
2.2 Potential Hazards and Safety Precautions
WARNING: Failure to follow the safety precautions listed below may result in property damage, personal injury, or even death.
2.2.1 General Precautions
Only qualified and authorized personnel should operate the equipment and must read this manual before proceeding
Prior to operating the equipment, fully understand and comply with all the applica-ble local safety by-laws, codes, and regulations
Be aware of the physical nature of the gases and fluids operating within the Charge Station. Consult your gas supplier and/or an applicable Material Safety Data Sheet (MSDS) for proper safety and handling procedures.
Become familiar with all fault features associated with the equipment
Wear protective eyewear and safety shoes when working around the equipment
Gases are to be plumbed in accordance with all applicable local safety by-laws, codes, and regulations
Do not use the Charge Station if damage to any of the components is suspected
Modifications should not be made to the equipment or any of its components for applications other than those specified by the manufacturer. Unauthorized modifi-cations can result in a dangerous shock hazard and can void the warranty
Inspect the equipment periodically: ensure that cables and wiring have not loos-ened up during operation and that all electrical connections are in place; use a hand-held sensor to check for hydrogen leaks from equipment piping
Do not operate the Charge Station in temperatures below 5 °C or above 40 °C
Do not store the Charge Station in temperatures below 5 °C
WARNING: Unauthorized modifications may result in unsafe operation, potentially dangerous electrical shock, explosion or burn hazards which could lead to damage to equip-ment, injury to persons or even death. Unauthorized modifications will void the warranty.
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL POTENTIAL HAZARDS AND SAFETY PRECAUTIONS
2.2.2 Mechanical and Handling Hazards
WARNING: Improper handling, operation, or maintenance of the equipment may cause per-sonal injury and also lead to equipment damage.The Charge Station system weighs approximately 250 kg. Attempting to lift it may present a serious risk of muscle strain or other personal injury.
Use appropriate safety equipment and lifting practices when installing or moving the Charge Station to another location.
2.2.3 Electrical Hazards
WARNING: High levels of voltage exist within the product that present a risk of electric shock. The 17-cell electrolyzer stack operates at up to 38 VDC and draws up to 202 Amperes. Due to the presence of residual reactants, the stack may continue to have a potentially dangerous electrical charge at its terminals, even after shutdown.
The cell stack must be disconnected from the power source, and purged with nitro-gen before any service is performed.
Do not touch the potentially high-voltage areas, such as the wiring harness, the stack termi-nals and the power cables..
Do not open the cabinet or touch any internal Charge Station components immediately after shut-down as voltage may still be present.
Do not short-circuit charged components of the stack with metal object.
Do not wear metal or electrically conductive jewelry while performing any service work on the equipment.
Ensure that the product is adequately earthed to protect against stray currents and static electricity hazards, in accordance with national codes and regulations.
2.2.4 High Temperatures
WARNING: Product surfaces and internal components can become hot and may cause severe burns. Ensure the Charge Station has completely cooled down before servicing.
Ensure the unit has cooled down before draining DI water from the system.
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POTENTIAL HAZARDS AND SAFETY PRECAUTIONS PEM ELECTROLYZER
2.2.5 Flammable Gas Atmosphere and Fire/Explosion Risks
WARNING: The hydrogen gas produced by the product may cause a fire or an explosion when exposed to heat, sparks or flames, or as a result of friction, especially in enclosed areas or under conditions of inadequate ventilation.
The process output of the Charge Station is hydrogen, which is a flammable, colour-less, odourless and tasteless gas. Hydrogen is non-toxic and cannot be detected by human senses. Hydrogen and air mixtures are highly combustible/explosive. A hydro-gen leak from any part of the equipment or its auxiliaries could create a combustion/explosion hazard.
Ensure that equipment containing hydrogen is adequately ventilated.
Electrically ground hydrogen-conveying equipment, water lines and vent stack, etc.
Keep all sources of ignition away. Prohibit open flames (smoking and welding) in a hydrogen area.
Maintain a positive pressure in hydrogen vessels to prevent the entry of air.
Periodically check for hydrogen leaks from the equipment piping using a hand-held sensor and/or SnoopTM. Hydrogen pressure should be monitored periodically.
See the Reference Documents section at the beginning of this manual for sourcing important reference materials concerning use and safe handling of hydrogen.
2.2.5.1 Action in the Event of FireThe most effective method to fight a hydrogen fire is to extinguish the source of hydro-gen supply, provided this can be done safely.
WARNING: Risk of explosion. Extinguishing a hydrogen fire while the source of hydrogen con-tinues to leak/flow can quickly create an explosive atmosphere more hazardous than the fire itself.
Where hydrogen cannot be isolated, do not extinguish the hydrogen fire while the flow of leaking hydrogen continues, as the danger of creating an explosion or an explosive re-ignition is a greater potential hazard than the existing fire.
Use water jets or sprays to cool surrounding equipment, especially pressurized hydrogen containers, during the fire, but DO NOT use water to extinguish the hydrogen fire directly.
Ensure that personnel responsible for operating the Charge Station and/or its related components are properly trained to respond to an emergency situation.
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL POTENTIAL HAZARDS AND SAFETY PRECAUTIONS
2.2.6 Enriched Oxygen Atmospheres
WARNING: The product produces oxygen as it operates. An oxygen enriched atmosphere rep-resents a hazardous condition and it is a serious physiological risk.
The equipment produces oxygen as it operates. The discharge from the anode system is pure oxygen.
Ensure that the Charge Station operates in an adequately ventilated environment.
Ensure that the hydrogen vent line is properly vented to the outdoors.
Periodically check for leaks from the equipment piping.
Oxygen and hydrocarbons (oil and grease) can react violently, potentially resulting in explo-sions , fire, injury and/or property damage. Never allow oil and grease to come in contact with oxygen under pressure. Even small amounts of hydrocarbons (or any organic matter) in the presence of high concentration, low pressure oxygen can be hazardous. Ensure that all tools, clothes, hands and personal protective equipment are free of organic oils and grease when servicing oxygen lines.
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POTENTIAL HAZARDS AND SAFETY PRECAUTIONS PEM ELECTROLYZER
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3 | Product OverviewThe Hylyzer Hydrogen Generator is a small-scale, modular electrolyzer which uses clean de-ionized water and electricity to produce up to 1.1 normal cubic metre per hour (Nm3/h) hydrogen. The electrolysis reaction takes place within a stack of 17 proton exchange mem-brane (PEM) cells. The Hylyzer Hydrogen Generator is built into a sturdy equipment cabi-net, and is designed to operate fully automatically once it has been started. Product features:
PEM electrolyzer stack
Cabinet mounted on wheels or adjustable feet
Indoor operation
Air cooled
Automatic operation - unit stops and restarts hydrogen production based on pressure of external hydrogen storage vessel/tubing.
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TECHNICAL SPECIFICATIONS PEM ELECTROLYZER
3.1 Technical Specifications
Table 3-1: Charge Station Technical Specifications
FCVM Cell Voltage Out of Limits (optional) De-oxo Overtemperature
FCVM Cell Voltage Offset Over-Limit (optional)
Air Flow
H2 in O2 detection Automatic Purge
Table 3-1: Charge Station Technical Specifications
PROPERTY UNIT VALUE
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TECHNICAL SPECIFICATIONS PEM ELECTROLYZER
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4 | InstallationThis section details the steps for receiving and installating the PEM Electrolyzer.
4.1 Environmental RequirementsThe PEM Electrolyzer is designed for indoor use. Please observe the following installation requirements:
It should be installed in a dry, clean, temperature-controlled environment ( 5–40°C).
Use only in a well-ventilated area, where the air is exchanged frequently.
Position the PEM Electrolyzer cabinet with space around it, so that its ventilation grilles will not become obstructed. Position the unit such that there is minimum 1 metre clearance front and back and 0.3 metres clearance on either side.
WARNING: The PEM Electrolyzer’s product oxygen is released within the cabinet. To prevent any potentially hazardous oxygen concentrations, all cabinet ventilation grilles must remain unobstructed and the PEM Electrolyzer must be run in a well venti-lated environment.
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UNCRATING AND INSPECTION INSTRUCTIONS PEM ELECTROLYZER
The combustible vent line must be run to the outdoors, as explained in Section 4.3.1.2 Combustible Vent on page 19.
4.2 Uncrating and Inspection InstructionsInspect the shipping container for damage. If the PEM Electrolyzer container has been dam-aged during shipment, immediately report it to Hydrogenics Corporation and the shipping per-sonnel. If there is no visible external damage, open the crate and remove all the packaging around the unit. Inspect the unit for any damage which may have occurred during transporta-tion.
CAUTION: If any damage is suspected, do not use the PEM Electrolyzer without the written approval of Hydrogenics Corporation.
Use a lifting device when moving the unit to another location (until it is unpacked and placed on its wheels, if provided in the order).
Once the PEM Electrolyzer is placed in its final position, lock the wheels.
Check the freeze indicator. If it indicates that the unit has been exposed to freezing tem-peratures immediately report the situation to Hydrogenics Corporation.
NOTE: If practical, please retain the original packing materials against the event that the unit may need to be returned to Hydrogenics for service or repairs.
4.3 PEM Electrolyzer ConnectionsThe unit connections can be divided into 3 main categories: process, power and diagnostic.
4.3.1 Process ConnectionsIn general terms, process connections are the points where fluids (DI water, hydrogen, oxygen) enter and/or leave the PEM Electrolyzer.
Process interconnect tubing should be SS316 rigid or flexible braided tube with an appropriate pressure rating (meeting local regulations) and compatible with the process fluid. With the exception of DI water feed/drain lines, PVC, teflon or other types of plastic tubes are not recom-mended. Process Interconnect tubing must be equal to or larger than the process interface fit-tings (no downsizing allowed)
Figure 4-1: Process Connections (typical)
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL PEM ELECTROLYZER CONNECTIONS
WARNING: All metal tubes must be connected to a common grounding system.
NOTE: The drain is only required when draining the unit for service. It is not used during oper-ation of the PEM Electrolyzer.
4.3.1.1 Hydrogen (H2) OutputA ¼” bulkhead compression fitting, 316SS, has been provided to connect to the hydrogen line.
Interconnect hydrogen tubing should be minimum 1/4”-.039 316SS.
4.3.1.2 Combustible VentA ¼” bulkhead compression fitting, 316SS, has been provided to connect to the combustible vent line. During operation a small amount of gas flows out of the vent to regenerate the dryer.
The vent line must run outside the building. Once outside, terminate the vent line with a goose-neck, to prevent rain from entering the line.
Place the output of the vent line away from any possible sources of ignition or other ventila-tion outputs (especially oxygen vents).
Place the output of the vent line such that it cannot exhaust on people or building surfaces.
When the PEM Electrolyzer is powered up, the hydrogen purge valve is automatically activated to purge the system and allow product gases to reach reasonable levels of purity. This purge valve is also activated during the shut-down procedure of the PEM Electrolyzer, or if there is an internal over-pressure.
4.3.1.3 DI Water SupplyThe DI water is used both to cool internal PEM Electrolyzer components and as the source for conversion to hydrogen and oxygen.
The customer must supply a source of DI water outside the PEM Electrolyzer cabinet. A ¼” bulkhead compression fitting, 316SS, has been provided to connect to the DI water input line. DI water input requirements are:
Consumption: 1.2 L/h
Flow rate: 1 L/min
Pressure: 10–100 psig
Temperature: 5 to 45 °C
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PEM ELECTROLYZER CONNECTIONS PEM ELECTROLYZER
There must be no oil or particulates present in the DI water stream. A minimum 10-micron filter should be used ahead of the DI water supply connection. The DI water quality must be at least 2 Mohm•cm.
4.3.1.4 DI Water DrainDI water is generally consumed by the electrolysis process. There is no need to drain water dur-ing operation; a permanent drain connection is optional.
When required for maintenance, the customer may drain the water into a pan or vessel. A ¼” bulkhead compression fitting, 316SS, has been provided to connect to the gravity fed DI water drain.
4.3.1.5 Leak Check and Nitrogen PurgeAfter installation of site interconnection tubing and hydrogen storage has been completed, a pressure test and leak test must be performed. The pressure and leak tests should follow local requirements. The PEM Electrolyzer is pressure tested at the factory and only requires a leak test.
A nitrogen purge of the hydrogen storage tank and adjacent tubing is mandatory every time the system components have been (or are suspected to have been) exposed to air. Typically a suc-cessful purge requires a dilution of oxygen content below the level at which a potentially flam-mable gas mixture exists. This level is known as the limiting or minimum oxygen concentration (MOC) and for hydrogen is typically taken as 4% oxygen by volume. A dilution below half of this level is generally accepted as safe.
For a typical storage system previously exposed to air (21% oxygen), this level can be achieved by pressurizing the system to ~30psig and then venting to ~7psig for a minimum 4 times. Dur-ing or after the pressurizing/ venting cycle, the pressure should never be allowed to drop to ambient.
4.3.2 Power ConnectionsThe PEM Electrolyzer must be supplied with a 200-250 VAC, 60 A, 1 phase 50/60Hz electri-cal connection.
Figure 4-2: Power Interface (right view)
Before connecting the PEM Electrolyzer to a power source, ensure the following:
All process/site interconnecting tubing is complete and pressure/leak tested (Section 4.3.1.5 Leak Check and Nitrogen Purge on page 20).
All site interconnecting H2 gas tubes and all H2 storage vessels have been purged with nitro-gen or other inert gas (Section 4.3.1.5 Leak Check and Nitrogen Purge on page 20)
PEM Electrolyzer is properly connected to a common grounding system as per application
All hand valves in normal operating position
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL STORING THE PEM ELECTROLYZER
DC power is provided to the PEM Electrolyzer via an Anderson SB3350 connector. The pinout is:
WARNING: DO NOT connect to a positive grounded system.
4.3.3 Diagnostic Connection (for service use only)A diagnostic port is located on the same panel as the power input. The mating Tyco connector part number is 796188-1 (connector qty 1) and 66399-3 (socket qty 2). Pin 14 is CAN H, pin 13 is CAN L. The port is only to be used by authorized service personnel.
4.4 Storing the PEM ElectrolyzerAlways store the PEM Electrolyzer in a heated (> 5°C) environment. If the unit is to be stored for an extended (non-operational) period:
Shut unit down and switch off the unit, then disconnect power.
Shut off and/or disconnect the DI water supply.
Isolate the hydrogen out line from the hydrogen storage vessel and vent the line.
Disconnect the hydrogen out line.
Drain the DI water from the system.
Replace any fluid and gas port caps.
CAUTION: The PEM Electrolyzer stack must be protected from freezing at all times: do not expose the PEM Electrolyzer to temperatures below 5 C. The maximum storage temperature for the PEM Electrolyzer is 40 C in a dry location.
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STORING THE PEM ELECTROLYZER PEM ELECTROLYZER
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5 | OperationThis section describes system functions and controls.
Once the PEM Electrolyzer has been installed and initialized, it can operate automatically indefinitely, as long as there is an uninterrupted supply of power, DI water and available hydogen storage capacity. The PEM Electrolyzer will produce gas until the line pressure reaches 100 psig (~790 kPa), at which point it will shut down. Once line pressure is reduced to a pre-defined setpoint, the PEM Electrolyzer will re-activate and continue to produce gas.
5.1 Pre-Operation ChecksPrior to starting the unit:
1. Remove the PEM Electrolyzer rear cover.
2. Ensure that all valves are set for normal operating position as follows:
DI tank drain hand valve (HV5001) closed, see Figure 5-1 Cell stack drain hand valve (HV5002) closed, see Figure 5-2 Deoxo heating coil hand valve (HV5003) open, see Figure 5-3
3. Ensure that the ventilation fan blades can spin freely and no debris is present in the radia-tor fan housing.
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PRE-OPERATION CHECKS PEM ELECTROLYZER
4. Replace the PEM Electrolyzer rear cover.
5. Ensure that the valves between the PEM Electrolyzer and the storage tank are open.
6. Ensure that the DI water supply valve is open and that the DI water system is operating.
CAUTION: Do not touch regulating valves PRV2023, PRV3004 or metering valves 2017 and 2018. These valves and regulators are factory set; changing their setpoints may lead to poor PEM Electrolyzer performance. If the setpoint of any of the valves has been accidentally altered, please see Section 6.2.8 Pressure Regulators Check on page 47and Section 6.3 Process Adjustment Procedures on page 77 for information on correct setting.
7. Check the H2 vent for blocakge.
Figure 5-1: DI Tank Drain Valve (HV5001)
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL PRE-OPERATION CHECKS
Figure 5-2: Cell Stack Drain Valve (HV5002)
Figure 5-3: De-oxo Heating Coil Valve (HV5001)
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CONTROL INTERFACE PEM ELECTROLYZER
5.2 Control InterfaceThe controls and displays, from left to right in Figure 5-4, are used as described in Table 5-1 below. Refer also to the state transition diagram,Figure 5-5: State Transition Diagram, on page 27.
Figure 5-4: PEM Electrolyzer Control Panel
WARNING: The On/Off switch is not sufficient for personal protection when servicing the PEM Electrolyzer. The PEM Electrolyzer must be properly disconnected/locked out/tagged out at a disconnect upstream of the On/Off switch.
Table 5-1 LED Legend
Control Function
Start Button (green)
The start button puts the system in the “Start Ready” state, which means that it will produce hydrogen whenever the pressure-activated demand switch allows (i.e., storage pressure is below activation set-point).
Stop Button (red)
The stop button shuts down the PEM Electrolyzer and returns the sys-tem to Standby State. It will not produce hydrogen again until Start is pressed.
Reset Button (blue)
Clears past faults and prepares system for initial operation. The Start button will not function until Reset has occured. Press Reset to put sys-tem in Standby state.
E-Stop (Emer-gency Stop, red)
The e-stop button shuts down the system as if there were a fault (to pre-Standby state) This button latches, and must be turned to be released before system will operate again
Hour Meter This counter indicates hours the system has been in operation.
Status Display The status display (HMI) will indicate the system’s current state or dis-play a fault message if any are in effect
On/Off Switch Main power switch. When this switch is off, all functions of the system are disabled. Turn On to initialize system.
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL CONTROL INTERFACE
Figure 5-5: State Transition Diagram
Init
Standby
Fill Water
Prime Pump
Polish Water Pressurize System
H2 Purge
Run
Estop
Temperature
Recovery
DI Water Tank Full(DI Water Tank High Level Switch = True &
Inlet Water Tank High Level Switch = True)
DI Water Flow OK
(DI Water Flow Switch = True for 10s)
Water Resistivity > 2MÙ
Cathode (H2) Pressure > 85psig
60s
Demand Switch = False
Anode/Cathode
Pressure < 20psig
& 30 more seconds
1036215 State Machine
& HWSS OK=True
2
1
5
6
7 8
9
1011
12
13
Start Ready
Cabinet Purge
3
4
Demand Switch = True
15s
Stack Temperature < 50°C
Stack
Temperature
> 65°C
30s & Anode/Cathode
Pressure < 20psig
Shutdown
Stop
Button
Pressed?
Yes
No
Power On
Reset ButtonEstop Button or Fault
Stop ButtonStart Button
Stop Button
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OPERATING PROCEDURE PEM ELECTROLYZER
5.3 Operating ProcedurePlease refer to the operational schematic in Figure 5-6 for the discussions in Sections 5.3.1 - 5.3.3.
Figure 5-6: Operational Schematic
5.3.1 InitializationTo set the system to automatic hydrogen production from Off:
1. Ensure unit is plugged in to power source, that DI water is connected and available, that Hydrogen output is connected to storage and that the combustible vent line is properly connected and running to the outdoors.
2. Turn On/Off Switch ON. The PLC and status display (HMI) will initialize.
3. Wait for the “Press Reset Button” message to appear on the HMI.
4. Press Reset Button. Doing so clears the PEM Electrolyzer safeties for operation.
5. Wait for the “System Standby - Press Start button to purge system” message to appear on the HMI.
DI Water tank
DI WATER INDI WATER PUMP
RECIRCULATION PUMP
O2 SEPARATORDRYER A DRYER B
DEOXOCELL STACKDC POWER SUPPLY
H2 BACKPRESS REG
O2 O2 BACKPRESS REGULATORREG
COOLING FAN
REGEN FLOW 20%
LIVE
SYSTEM INITIALIZINGPRESS RESETPRESS STARTCABINET PURGEPRIME PUMPPRESSURIZINGHYDROGEN PURGERUNFILL WATERWATER POLISHING
HYDROGENICS
STSSTORAGE TANK
START STOP RESET E-STOP
PURGE FAN
H2 VENT
FAN CYCLE
SEPARATOR CYCLE
DI TANK CYCLE
SW DRY
O2 VENTNEXT SLIDE
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6. Press Start Button.
Once the start command is received, the status display (HMI) will display the following status sequence:
Cabinet Purge: This is intended to remove any hydrogen that may have accumulated inside the process compartment due to a hydrogen leak while the PEM Electrolyzer was in standby. The cabinet purge fan will run while HMI displays "PURGE CABINET". If the air-speed sensor does not read between factory set minimum and maximum values, the HMI will display “AIR FLOW SPEED SENSOR OUT OF RANGE”. If the air flow speed is within range but the air flow speed is too low for a specific period of time (both speed and time limits are factory default settings), the HMI will display "AIR FLOW SPEED UNDER LIMIT”.
DI Water Fill: If the DI water tank is empty, the DI water feed solenoid valve SV4003 will open; otherwise this step will be skipped. Once DI water tank has filled, the DI water feed pump PMP1000 will turn on and solenoid valve SV1127 will open to fill the oxygen separa-tor TK1002. The HMI displays "FILL WATER".
Prime Pump: When oxygen separator is full, the water circulation pump PMP1003 starts and the HMI will show the "PRIME PUMP" message while the electrolyzer waits for a steady flow confirmation. During this step the pump can cycle (start and stop) several times if the steady circulation flow is not confirmed within a certain time. If the maximum number of cycles is reached without steady flow being established, the system will fault and the HMI will display the "FAIL TO PRIME PUMP" fault message.
Polishing Water: Once the steady flow has been established, the DI water resistivity is checked. If found less than 2 MΩ ·cm, the system will continue to circulate water via the cell stack circulationloop in an attempt to improve it. During this time, the HMI will display the "POLISH WATER " message. If DI water quality fails to improve within a certain time, the system faults and the HMI displays "FAIL TO POLISH WATER". If water resistivity is greater than 2 MΩ ·cm then this step is skipped.
Pressurization: Once DI water resistivity is > 2 MΩ ·cm, the cell stack is energized, gener-ating hydrogen and oxygen. System pressure starts rising; the HMI displays "PRESSURIZE SYSTEM”. The PEM Electrolyzer must pressurize to a preset pressure in a certain time oth-erwise it will fault and the HMI will display "FAIL TO PRESSURIZE SYSTEM”.During this step the differential pressure control is active. It is very important to maintain differential pressure within specific limits in order to preserve the PEM membrane integrity. Differential pressure is maintained by:
-active control at process level by the means of oxygen backpressure regulating valve PRV3004, dome loaded hydrogen backpressure regulating valve PRV2007 (reference pressure set by oxygen pressure) and non return valve CHK2037. The PRV3004 sets the cell stack pressure. This same pressure is being applied to the dome of hydrogen back-pressure regulating valve PRV2007, ensuring the set point of the two PRVs is actively bal-anced.-reactive control by triggering the Emergency Shut Down mechanism based on oxygen and hydrogen pressure transmitters (PT1010 and PT1100 respectively) when the low or high pressure differential limits are reached. The HMI displays (respectively) "DIFFEREN-TIAL PRESSURE LOW" or "DIFFERENTIAL PRESSURE HIGH".
In normal operation some hydrogen is evacuated from the PEM Electrolyzer during the short pressurization phase through the hydrogen vent stack.
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H2 Purge: Once pressurized, the PEM Electrolyzer begins the hydrogen purge phase. The HMI displays "PURGE HYDROGEN". The pressure continues to rise to the point set by PRV2007 (implicitly by PRV3004). Once set point pressure has been reached the oxygen starts flowing out and pressure is maintained at a constant value (normal set in the range of 100-115 psig). Simultaneously, the hydrogen pressure rises to the same value and the hydrogen is conveyed via oxygen removal reactor (Deoxo) R2009, and dryers VSSL2014 and VSSL2015 (first through dryer VSSL2014, then dryer VSSL2015) to the hydrogen vent stack (dryer depressurization valves are open during this phase). The non return valve CHK2036 ensures a positive relative pressure in the purification system so air cannot re-enter even if solenoid valves SV2014 and SV2018 are open.
Run: After the PEM Electrolyzer has been purged, the system advances to hydrogen pro-duction. The HMI displays “SYSTEM RUNNING”. Hydrogen and oxygen pressure is bal-anced as described above with hydrogen pressure 0.5-5psig higher than oxygen pressure. This prevents oxygen from migrating into the hydrogen stream. Conversely, hydrogen-in-oxygen crossover leaks are detected by hydrogen detector GD1000. A reading greater than 40%LFL (1.6 % by volume) or a defective sensor will trigger an Emergency Shut Down.
The hydrogen flows into Oxygen Removal Reactor R2009. Here a very small amount of hydrogen is recombined with any residual oxygen forming water. The reaction requires a palladium based catalyst found in the Oxygen Removal Reactor (Deoxo). After passing through the Deoxo vessel, hydrogen enters the dryers where moisture content is dropped down to 15 ppm.
5.3.2 Dryer OperationDrying of the hydrogen stream occurs by pressure swing adsorption. Drying vessels VSSL2014 and VSSL2015 are filled with an alumina based desiccant (molecular sieve) that captures moisture from hydrogen stream. In principle one dryer is active at a time while the other is regenerating. Regeneration of desiccant is necessary to release mois-ture trapped during the active phase.
The 3-way valve SV2012 initially directs hydrogen towards dryer VSSL2014. The hydro-gen flows from Deoxo into dryer VSSL2014 for 15 minutes, exiting with less than 15 ppm moisture content. Regeneration valve SV2014 is kept closed (energized) as long as dryer VSSL2014 is active.
Approximately 80% of the hydrogen flow will be directed to the user line via 3-way valve SV2013 and dryer backpressure regulating valve PRV2023. PRV2023 ensures that pressure in the active drying vessel is maintained at 85-95 psig (necessary for adsorp-tion to occur). However, the PRV2023 setpoint must be lower than that of PRV3004 in order to keep the oxygen and hydrogen pressures balanced.
The remaining 20% of the hydrogen flow is directed to dryer VSSL2015 (now in regen-eration) via metering valve OR2017 and then out to the vent stack via open (de-ener-gized) regeneration valve SV2018. Regeneration of dryer VSSL2015 happens at low pressure (1-3psig) over a 10 minute period. After 10 minutes, regeneration valve SV2018 will close (energize) and the vessel will pressurize (while regeneration flow through OR2017 slowly drops) until it reaches the same pressure as active drying vessel
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VSSL2014. When pressure in the two dryers is balanced, the regeneration flow stops and dryer VSSL2015 remains pressurized until the end of active phase of dryer VSSL2014. Total pressurization and standby time of dryer VSSL2015 is 5 minutes.
After 15 minutes the two drying columns reverse roles: dryer VSSL2014 goes into regeneration while dryer VSSL2015 becomes active. Figure 5-7 illustrates the dryers’ operation and pressurization/depressurization cycle.
Figure 5-7: Dryer Cycling
Zone A: Drying column A is active and fully pressurized. 100% of hydrogen pro-duced by the cell stack flows through. Drying column B is in regeneration at low pressure. 20% of the already dry hydrogen flow (from downstream drying column A) passes through and then out to the vent stack. This flow is wasted to atmo-sphere.
Zone B: Drying column A is active and fully pressurized. 100% of hydrogen pro-duced by the cellsatck flows through. Drying column B is in regeneration but the regeneration valve (SV2018) is now closed and pressure is rising while regeneration flow is dropping from 20% to zero. It will reach full pressure in less than 5 minutes.
Zone C: Drying column A is active and fully pressurized. 100% of hydrogen pro-duced by the cellsatck flows through. Drying column B is pressurized at full pres-sure and in standby. At this point, 100% of cell stack hydrogen produced is directed to the user line.
The next three phases (zones D, E and F) mirror the first three (zones A, B and C respec-tively)
Zone D: Drying column B is active and fully pressurized. 100% of hydrogen pro-duced by the cell stack flows through. Drying column A is in regeneration at low pressure. 20% of the already dry hydrogen flow (from downstream drying column B) passes through and then out to the vent stack. This flow is wasted to atmo-sphere.
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Zone E: Drying column B is active and fully pressurized. 100% of hydrogen pro-duced by the cellsatck flows through. Drying column A is in regeneration but the regeneration valve (SV2014) is now closed and pressure is rising while regeneration flow is dropping from 20% to zero. It will reach full pressure in less than 5 minutes.
Zone F: Drying column B is active and fully pressurized. 100% of hydrogen pro-duced by the cellsatck flows through. Drying column A is pressurized at full pres-sure and in standby.
5.3.3 Continuous OperationAfter passing through the purification system (Deoxo and drying vessels) the hydrogen stream is directed to the user via backpressure regulating valve PRV2023 and solenoid valve SV2019.
Unit will remain in "RUN" state for as long as user line pressure is below the pressure switch PS2026 high setpoint. (also referred to as automatic shutdown pressure). This is factory set to 100psig but may be altered within certain limits at customer request. Once the pressure high setpoint is reached the PEM Electrolyzer shuts down and the shutdown depress is activated. The HMI displays "SHUTDOWN - WAIT FOR SYSTEM DEPRESSURIZATION”.
Once the shutdown phase is complete, the PEM Electrolyzer goes to standby. It remains in standby for as long as user line pressure is above the lower setpoint of pres-sure switch PS2026 (also referred to as automatic restart pressure). This is factory set to 60psig but may be altered within certain limits at customer request. The HMI displays "SYSTEM READY WAIT FOR DEMAND". Once user line pressure pressure drops below automatic restart pressure, the unit restarts and runs the cycle described above.
5.4 Shutdown Procedure1. Press Stop Button.
2. Wait for display to read “System in standby”.
3. Shut off power switch.
4. Shut off water.
5. Shut off hydrogen line.
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6 | General MaintenanceRegular inspection and maintenance must be performed to maintain the PEM Elec-trolyzer in optimal working condition and prolong the life of its components. Addi-tionally, the operating times must be logged for the purposes of meeting maintenance intervals as outlined in this section.
The systems and equipment shall be operated and maintained by qualified and authorized personnel only. Personnel responsible for operating or maintaining the equipment described in this manual must:
Read, understand and comply with the instructions presented throughout this manual;
Read the “Safety Information” section of this manual in order to understand the potential hazards associated with the systems or equipment.
Fully understand and comply with all applicable local safety by-laws, codes, and regulations.
Be trained in working with live electrical circuits.
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6.1 Maintenance Intervals and Spare PartsInspection and service intervals are specified below.
Table 6-1Maintenance Intervals
MAINTENANCE ITEM SECTION HYG P/N JAN
FEB
MA
R
AP
R
MA
Y
JUN
JUL
AU
G
SEP
OC
T
NO
V
DEC
Check H2 vent stack X X X X X X X X X X X X
Check E-stop operation 6.2.2 X X X X X X X X X X X X
Check Fault Log for past month X X X X X X X X X X X X
Check for Gas leaks 6.2.3 X X
Clean / check rad fan operation 6.2.4 X X
Check tubing and pipe supports X X
Check H2 area detector 6.2.5 1031226 X X
Check equipment (connected to a common ground)
6.2.9 X X
Replace FLT2004filter element 6.2.6 1005300 X
Check air flow switch 6.2.7 X
Replace H2 area detector 6.2.5 1031226 X
Check all regulator settings 6.2.8 X
Check AC and DC power cables / connections
6.2.9 X
Check drain trap DT2004 6.2.10 1018604 X
Check DC voltage / current sensors 6.2.11 2000902/1027409
X
Check pressure transducers 6.2.12 2000075 X
Check / replace solenoid valvesa See Note a X
Check / replace DI bed 6.2.14 1020583 3000 hoursb
Check / replace dryer desiccant 6.2.14 2003448 4 years
Run test X X X X X X X X X X X X
a. Normally open (SV2014, SV3018, SV3005) P/N: 1036463; Normally closed (SV1127, SV4003) P/N: 1039043; 3-way (SV2012, SV2013) P/N: 1036358
b. Varies with feed water quality
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6.2 Maintenance ProceduresThe following maintenance procedures explain how to access parts to perform the inspections and replacements mentioned in Section 6.1 Maintenance Intervals and Spare Parts on page 34.
6.2.1 CleaningUse mild cleansers (soap and water) and a damp cloth to clean the exterior covers of the PEM Electrolyzer if cleaning is required.
6.2.2 E-stop Operation CheckIn order to ensure that the PEM Electrolyzer can be manually stopped in event of an emergency, the operation of the E-stop button should be checked regularly as per the maintenance schedule in section 6.1.
6.2.2.1 Tools Required
None
6.2.2.2 Personal Protective Equipment
Safety glasses
6.2.2.3 Steps
1. Turn power on and bring unit to run state (displayed on HMI)
2. Allow PEM Electrolyzer to run for 10 minutes
3. Press E-stop. The PEM Electrolyzer should shut down instantaneously and display the E-stop condition on the HMI
4. Allow 4-10 min for depressurization
5. Reset E-stop push button (by rotating/pulling out) and then press the Reset push button. Observe that the E-stop condition has been cleared (on HMI).
Apply the same steps to every other E-stop push button installed. After all E-stop but-tons have been checked and functionality has been confirmed, run the PEM Electrolyzer for at least 10-15 additional minutes and then set up for automatic operation.
Please note that if user line has been previously pressurized above the production auto-matic restart set point the PEM Electrolyzer will not run. The HMI display will show the "Wait for demand switch" message.
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6.2.3 Gas/Water Leak Check
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter. Use personal protective equipment.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
6.2.3.1 Tools Required
Swagelok SNOOP or equivalent leak testing fluid
Open wrench (9/16”, 11/16”, 7/8”)
6.2.3.2 Personal Protective Equipment
Safety glasses
Safety shoes
6.2.3.3 Leak Check Steps
1. Switch power off and remove unit back cover
2. Apply SNOOP liquid to the fitting(s) suspected of leaking
3. Turn power to the unit on and start unit up. Allow unit to reach run status and to pressurize
4. Check fitting(s) under test for leaks (bubbles and/or foam formation). If a leak has been detected, stop the unit and allow the PEM Electrolyzer to completely depres-surize and for the electrolyzer stack to electrically discharge. Proceed with tighten-ing fittings only once you are certain that the PEM Electrolyzer has been completely depressurized and stack discharged
5. Repeat the above steps in order to verify that the leak has stopped
6. Reinstall back cover and set the PEM Electrolyzer for automatic operation.
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NOTE: In some cases removal of respective subassembly will be necessary in order to fix the leak.
NOTE: Water leaks are visible without use of Snoop leak detector liquid.
6.2.4 Check/Clean Radiator and Ventilation FansRadiator fans and ventilation fans are located inside the process compartment and the electrical compartment.
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
6.2.4.1 Tools Required
Brush
Compressed Air
6.2.4.2 Personal Protective Equipment
Safety glasses
Dust mask
Safety shoes
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6.2.4.3 Checking Steps
1. Make sure that the PEM Electrolyzer has been switched off and power locked out
2. Remove PEM Electrolyzer back cover and open electrical cabinet doors
3. Visually inspect radiators and fans for dust, debris and blade condition. Turn blades by hand to verify free movement
4. Turn power on and run unit. Verify if ventilation fans are running. During run mode verify that water cooling radiator fan cycles
5. Switch unit off, reinstall back cover and close electrical cabinet doors.
6. Run unit again and set for automatic operation.
6.2.4.4 Cleaning Steps
1. Make sure that the PEM Electrolyzer has been switched off and power locked out
2. Remove PEM Electrolyzer back cover and open electrical cabinet doors
3. Remove radiator fan guard
4. Remove any debris from inside radiator fan housing
5. Blow radiator fins clean using a brush and compressed air
6. Reinstall fan guards
7. Turn power on and run unit. Verify if ventilation fans are running. During run mode verify that water cooling radiator fan cycles
8. Switch unit off, reinstall back cover and close electrical cabinet doors.
9. Run unit again and set for automatic operation.
6.2.5 Hydrogen Gas Detector Check
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
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WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
WARNING: Use of other than oxygen compatible lubricants on oxygen service lines is a serious hazard. Spontaneous combustion can occur. Ensure that your hands are clean and free of organic grease or lubricants when servicing oxygen lines. Do not use tools or equipment contaminated by orgainc grease or lubricants.
6.2.5.1 Tools Required
Open wrench 9/16”
Span gas kit (50% and 20% LEL H2 in air span gas, pressure reducing head 2 L/min minimum flow rate, hose), both shown below
Figure 6-1: Span Gas Kit
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Figure 6-2: Span Gas Cylinder Hose
6.2.5.2 Personal Protective Equipment
Safety glasses
Safety shoes
6.2.5.3 Hydrogen Gas Detector Check Steps
1. Switch power off and remove unit back cover
2. Remove tube connection between PRV3004 and OR2018 (PID dwg 1038516 rev 3)
Figure 6-3: Hydrogen Tube Disconnection
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3. Connect the pressure reducing head to 20% LEL span gas cylinder and attach one end of the hose to the cylinder. Connect the other end of the hose in place of the tube that was just removed from PRV3004
Figure 6-4: Span Gas Hose Attachment to Cylinder
4. Make sure that the end tube located in front of the hydrogen gas detector (GD1000, PID dwg 1038516 rev3) lines up with H2 sensor circular orifice
Figure 6-5: Hydrogen Tube Alignment with Sensor
5. Turn power on and after HMI initializes press Reset push button. DO NOT PRESS START PUSH BUTTON as unit must NOT RUN
6. Apply 20 %LEL span gas by turning span gas cylinder valve on and allow a couple of minutes for sensor response
7. Observe that the hydrogen gas detector status LED indicates a warning condition. This warning condition must not induce an E-STOP status on HMI
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8. Repeat these steps using 50%LEL span gas
9. Observe that the hydrogen gas detector status LED indicates a fault condition and also HMI indicates the E-STOP status.
10. Remove test kit and reinstall the ¼ inch stainless steel tube between PRV3004 and OR2018
11. Reinstall back cover, reset and restart unit. After 10-15 min unit can be set for auto-matic operation.
6.2.6 Oxygen and Hydrogen Filter Elements Replacement
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
WARNING: Use of other than oxygen compatible lubricants on oxygen service lines is a serious hazard. Spontaneous combustion can occur. Ensure that your hands are clean and free of organic grease or lubricants when servicing oxygen lines. Do not use tools or equipment contaminated by orgainc grease or lubricants.
6.2.6.1 Tools Required
Open wrench (9/16”, 11/16”, 7/8”)
Strap wrench
Shop cloth or paper towel
6.2.6.2 Personal Protective Equipment
Safety glasses
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6.2.6.3 Filter Replacement StepsThe following replacement steps apply to both the O2 and H2 filters. The figures below show the O2 filter.
1. Locate the red oxygen filter (FLT3007) as shown in Figure 6-6. An identical filter has been installed on hydrogen line (FLT2004). Record the housing inlet and outlet ori-entations.
Figure 6-6: Oxygen Filter Location
2. Carefully remove the drain line shown in Figure 6-7 below (make sure not to break the transparent water trap). DI water may drain from the filter. Wipe it dry using a clean cloth or paper towel. Undo inlet and outlet compression fittings and remove filter body from the unit
Figure 6-7: DI Filter Housing
3. Once filter is out, unscrew the filter from its head. This can be done by hand or using a strap wrench. Inspect the seal ring and replace if damaged in any way.
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4. Unscrew the filter element holder as shown in Figures 6-8 and 6-9 and remove the filtration element. Replace the element and reinstall filter holder following the same steps in reverse order. Hand tighten the filter holder ahd filter body. Do not use tools. Do not overtighten the filter element holder; doing so may damage the filter element and/or threads. Do not overtighten filter body or compression fit-tings. Ensure the housing is re-installed in the same orientation as found in step 1.
5. Perform a leak check as per Section 6.2.3 Gas/Water Leak Check on page 36.
CAUTION: Do not use any grease or lubricants on fittings, filter, filter element or any other part that may come in contact with oxygen gas. New or contaminated fittings, filter body and/or tubing must be oxygen cleaned before installation.
Figure 6-9: Oxygen (Hydrogen) Filter and Housing Components
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6.2.7 Air Flow Speed Sensor Check
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
6.2.7.1 Tools Required
None
6.2.7.2 Personal Protective Equipment
Safety glasses
Safety shoes
6.2.7.3 Air Flow Speed Sensor Check Steps
1. Switch power off and remove unit back cover
2. Locate the electrical connector of the enclosure purge fan and disconnect so that the enclosure purge fan cannot run. The electrical connector can be found on or close to the fan mounting bracket by tracing the fan power feed wire (see Figure 6-10)
3. Air speed sensor is located behind the cabinet purge fan (see Figure 6-11)
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Figure 6-10: Air Speed Sensor Disconnect
Figure 6-11: Air Speed Sensor Location
4. Turn power on and start up the unit. On the HMI observe that unit goes in "cabinet purge" status
5. After 60 seconds the air flow speed out of range is shown on the HMI and the unit will stop
6. Reconnect the air speed sensor electrical connector
7. Reinstall back cover, reset and restart unit. After 10-15 min unit can be set for auto-matic operation
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6.2.8 Pressure Regulators Check
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
WARNING: Use of other than oxygen compatible lubricants on oxygen service lines is a serious hazard. Spontaneous combustion can occur. Ensure that your hands are clean and free of organic grease or lubricants when servicing oxygen lines. Do not use tools or equipment contaminated by orgainc grease or lubricants.
6.2.8.1 Tools Required
Monitoring software
0-150psig pressure gauge
Open wrench 9/16”
¼” compression union cross (Swagelock P/N SS-400-4)
¼” SS316 compression nuts and ferrules (2 sets)
¼” SS316 x 0.035 tube (0.3meters)
6.2.8.2 Personal Protective Equipment
Safety glasses
Safety shoes
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6.2.8.3 PRV3004 Setpoint Adjustment
1. Connect monitoring software and confirm internet connection
2. Ensure the PEM Electrolyzeris completely depressurized
For units without dryer pressure indicator:
3. Switch power off and lock/tag out main disconnect
4. Remove back cover of the unit
5. On the most accessible dryer, remove outlet ¼“ compression "T" union (Figure 6-12) and replace with ¼“ union cross compression (Figure 6-13). Reconnect adja-cent tubing and connect the pressure gauge to the open port of the union cross (Figure 6-13). Make sure all compression nuts are properly swaged
Figure 6-12: Dryer Outlet ¼“ Compression "T" Union
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Figure 6-13: Pressure Gauge Connection to ¼“ Compression Cross Union
6. Turn power to the unit back on and bring the monitoring software on line
For all units:
7. Start up unit and allow at least 15 min of operation
8. Using monitoring software read oxygen pressure (under "System" screen). This pressure must be in the range of 100-115psig. If the pressure is lower than 100 psig, adjust the set screw of PRV3004 (PID dwg 1038516 rev3) by slowly turning it clock-wise till the desired pressure has been reached. Run PEM Electrolyzer for a couple minutes to make sure that pressure reading stabilizes to the proper value. Readjust setpoint if necessary.
CAUTION: Regulator PRV3004 must be set for higher pressure than regulator PRV2023 at all times otherwise damage or underperformance of the system will occur.
9. There are 2 drying columns, each running 15 minute drying cycles. While one dryer is running an active drying cycle, the second runs a 10 minute regeneration plus 5 minute pressurization cycle. Every 15 minutes, the dryers switch cycles such that the dryer that was active goes into regeneration and vice versa.
6.2.8.4 PRV2023 Setpoint AdjustmentPRV 2023 (PID dwg 1038516 rev3) can be adjusted similarly to PRV3004 (described in Section 6.2.8.3 above). However, the setpoint must be 85-95 psig and the reading should be taken from the dryer pressure gauge. For units without a manufacturer installed pressure indicator, use the test gauge that was used for the PRV3004 setpoint adjustment (Figure 6-13) and wait for the respective dryer to become active.
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NOTE: During dryer operation, pressure will "swing" from one dryer to the other so that at times only one dryer is pressurized. There is also a pressurization phase when pressure raises from 0 to maximum set by PRV2023 for each dryer and cycle. Set point adjust-ment has to be made and pressure reading must be taken when dryer fully pressurized! For units with no factory installed pressure indicator this must be done during drying phase of the dryer on which the test pressure indicator was installed.
For units without dryer pressure indicator:
1. When PRV2023 has been properly set, stop PEM Electrolyzer operation by pressing Stop push button and allow time for the unit to fully depressurize (pressure can be checked on line using monitoring software). Remove test gauge and union cross and reconnect all tubing as per manufacturer original build.
For all units:
2. Reinstall unit back cover
3. Restart electrolyzer and allow minimum 15 minutes operation before setting it for automatic run
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6.2.9 Cell Stack DC Cable Connection and Equipment Grounding/Bonding Check
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
6.2.9.1 Tools Required
None
6.2.9.2 Personal Protective Equipment
Safety glasses
Safety shoes
6.2.9.3 Electrical Connection Check
1. Switch power off and lock/tag out main disconnect. Cell stack must be completely free from any residual electrical charge and at rom temperature.
2. A visual inspection must check but shall not be limited for imperfect electrical con-tact, oxidized contacts/wire, loose cable strands, broken wire, insulation conditions, signs of overheating, etc.
3. Check all electrical connections for tightness.
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6.2.10 Drain Traps DT 2004 and DT3006 Check
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
WARNING: Use of other than oxygen compatible lubricants on oxygen service lines is a serious hazard. Spontaneous combustion can occur. Ensure that your hands are clean and free of organic grease or lubricants when servicing oxygen lines. Do not use tools or equipment contaminated by orgainc grease or lubricants.
6.2.10.1Tools Required
None
6.2.10.2Personal Protective Equipment
Safety glasses
Safety shoes
6.2.10.3Drain Trap Check
1. Confirm that the PEM Electrolyzer has run for at least 100 hours total (not necessar-ily continuous) since the last drain trap check/cleaning. Run time is recorded on the hour meter mounted control panel (Figure 5-4).
2. Switch power off and lock/tag out main disconnect. Cell stack must be completely depressurized and free from any residual electrical charge.
3. Remove unit back cover.
4. Locate drain traps (Figures 6-14 and 6-15) and visually inspect the water level inside them. There must be some water inside each drain trap but the level must not be to
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the point where the float actuates the drain valve. If a drain trap is dry then the seat of the float valve may not be sealing properly. Further possible symptoms are low production rate; low oxygen and/or hydrogen pressure, failure to pressurize unit and/or high/low pressure differential. If drain trap is completely full with water than a failed closed float valve or drain tube blockage can be suspected. Further possible symptoms are: wet/saturated oxygen and/or hydrogen gas, water carry over in gas lines, poor Deoxo and Dryer Columns performance, high/low pressure differential.
Figure 6-14: Drain Trap
Figure 6-15: Drain Trap
5. Re-install the back cover.
6. Run unit and set up for automatic operation.
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6.2.11 Current Sensor CM1500 and Voltage Sensor VM1500 Check and Replacement
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
6.2.11.1 Tools Required
DC current clamp meter (0-250 A, calibrated)
DC voltmeter (0-50Vdc, calibrated)
Monitoring software
6.2.11.2Personal Protective Equipment
Safety glasses
Safety shoes
Electrician gloves
6.2.11.3Current Sensor and Voltage Sensor Check
1. Switch power off and lock/tag out main disconnect. Cell stack must be completely depressurized and free from any residual electrical charge.
2. Remove back cover of the unit.
3. Install clamp meter on the stack positive or negative power cable (Figure 6-16). Consider electrical power flow through the stack when deciding the orientation (polarity) of clamp meter.
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Figure 6-16: Cell Stack Current Measurement using Clamp Meter
4. Turn power back on and make sure that monitoring software runs on line.
5. Turn unit on and allow it to reach run state.
6. Record the clamp meter current measurement and monitoring software current measurement (Figure 6-17 - current measurement). The load can be adjusted using the on board potentiometer (see Figure 6-39 on page 79).
7. Compare the two readings. The software current measurement must be within +/- 3% of the clamp meter measurement.
Figure 6-17: System Monitoring Software Current/Voltage Measurement
8. Repeat this procedure for a lower load (e.g. 80A).
9. Turn power back on and make sure that monitoring software runs on line.
10. Turn unit on and allow it to reach run state.
Voltage Measurement
Current Measurement
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11. Run unit at full load.
12. Measure and record voltage across cell stack power terminals (Figure 6-18). Record the monitoring software DC voltage reading (Figure 6-17 - voltage measurement).
Figure 6-18: Cell Stack Voltage Measurement
13. Compare the two readings. The software voltage measurement must be within +/- 1% of the voltmeter measurement.
14. Repeat this procedure for a lower load (e.g. 80A).
15. Shut power off and disconnect from power source. Lock out disconnect and tag. Allow time for unit depressurization and stack discharge.
16. Re-install the back cover.
17. Run unit and set up for automatic operation.
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6.2.12 Pressure Transmitter Check
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
WARNING: Use of other than oxygen compatible lubricants on oxygen service lines is a serious hazard. Spontaneous combustion can occur. Ensure that your hands are clean and free of organic grease or lubricants when servicing oxygen lines. Do not use tools or equipment contaminated by orgainc grease or lubricants.
6.2.12.1Tools Required
Monitoring software
0-100psi pressure gauge
Open wrench 9/16”, 11/16”, 7/8”
100 psi nitrogen supply
Shop cloth or paper towel
Flexible tubing and fittings rated for 200 psi
6.2.12.2Personal Protective Equipment
Safety glasses
Safety shoes
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6.2.12.3Pressure Transmitter Check
1. Switch power off and lock/tag out main disconnect. Cell stack must be completely depressurized and free from any residual electrical charge.
2. Remove load side wires of contactor CT318 and isolate. This is to prevent cell stack for being accidentally energized during test.
5. Identify oxygen (PT1010) and hydrogen (PT1100) pressure transmitters (Figure 6-20). Label transmitters and their corresponding electrical connectors (socket) accordingly.
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Figure 6-20: Pressure Transmitters
6. Disconnect electrical connectors and remove transmitters from installation. Some DI water may drain at the point of process fitting disconnect.
7. Connect the transmitters and pressure calibrator to a common pressurized nitrogen source. All three instruments must "see" same pressure during test (Figure 6-21).
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Figure 6-21: Pressure Transmitters and Calibrator connected to common pressure
8. Reconnect the two pressure transmitters to their respective electrical connectors.
9. Turn power back on and make sure that monitoring software runs on line. Bring the PEM Electrolyzer to standby status by pressing the "Reset" button on the con-trol panel (Figure 5-4).
Important: Do NOT press START button at any time during test. PEM Electrolyzer MUST be in "STANDBY" state for the entire duration of the test.
10. Apply zero pressure to both pressure transmitters and pressure calibrator. Record the monitoring software oxygen and hydrogen pressure readings (Figure 6-22).
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Figure 6-22: System Monitoring Screen
11. Record the pressure calibrator reading and compare with pressure transmitter read-ings. Each pressure transmitter reading must not deviate with more than +/-0.3 psi from the pressure calibrator reading. Regardless of the pressure calibrator reading, the difference between the two pressure transmitter readings must be no greater than 0.3 psig.
12. Repeat the test procedure by applying 100 psig nitrogen pressure to the pressure calibrator and the two pressure transmitters.
13. If any of the pressure transmitters does not pass the check up criteria please contact Hydrogenics Customer Service (Section 1.3 Customer Assistance on page 2).
14. After test completion, turn power off, lock out electrical disconnect and tag.
15. Remove test rig. Reinstall pressure transmitters in their original location. Ensure that all fittings are properly tightened.
16. Reconnect the two pressure transmitter electrical connectors. Reconnecting con-tactor load wires.
17. Start up the unit and monitor for leaks. If any leaks are found, fix them according to Section 6.2.3 Gas/Water Leak Check on page 36.
18. When all leaks are fixed, disconnect unit from power, lock out disconnect and tag. Allow cell stack to electrically discharge.
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
WARNING: Use of other than oxygen compatible lubricants on oxygen service lines is a serious hazard. Spontaneous combustion can occur. Ensure that your hands are clean and free of organic grease or lubricants when servicing oxygen lines. Do not use tools or equipment contaminated by orgainc grease or lubricants.
6.2.13.1Tools Required
Bench vise
Flat head screwdriver
Small adjustable wrench, open wrenches of various sizes
INSTALLATION, OPERATION AND MAINTENANCE MANUAL MAINTENANCE PROCEDURES
6.2.13.3Solenoid Valve Maintenance
WARNING: To prevent the possibility of personal injury or property damage, turn off electrical power, depressurize valve and vent fluid to a safe area before servcing the valve.
CleaningAll solenoid valves should be cleaned periodically. The time between cleaning will vary depending on the medium and service conditions. In general, if the hvoltage to the coil is correct, sluggish valve operation, excessive noise or leakage will indicate that cleaning is required. In the extreme case, faulty valve operation will occur and the valve may fail to shift. Clean strainer or filter when cleaning the valve.
Preventative Maintenance
Keep the medium flowing through the valve as free from dirt and foreign material as possible.
While in service, the valve should be operated at least once a month to ensure proper opening and closing.
Depending on the medium and service conditions, periodic inspection of internal valve parts for damage or excessive wear is recommended. Thoroughly clean all parts. If parts are worn or damaged, install a complete ASCO Rebuild Kit.
Causes of Improper Operation
Incorrrect Pressure: Check valve pressure. Pressure to valve must be within range specified on nameplate.
Excessive Leakage: Disassemble valve and clean all parts. If parts are worn or dam-aged, install a complete ASCO Rebuild Kit.
Valve Disassembly
1. Switch power off and lock/tag out main disconnect. Cell stack must be completely depressurized and free from any residual electrical charge.
2. Remove unit back cover.
3. Remove valve to be serviced from PEM Electrolyzer.
4. Disassemble valve in an orderly fashion using exploded views for identification and placement of parts.
5. Secure valve in a bench vise and pop solenoid retention red cap and retention plate using the screwdriver (Figures 6-23 and 6-24). Some valves have solenoid retained by a nut; in this case, unscrew the nut.
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Figure 6-23: Solenoid valve disassembly
Figure 6-24: Solenoid valve disassembly (cont’d)
6. Remove solenoid and retention spring (if installed) (Figures 6-25, 6-26 and 6-27) and unscrew the solenoid base subassembly. Take care not to lose inside springs.
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7. The remaining disassembly steps depend on the solenoid type.
ASCO Series 8223
1. Unscrew solenoid base subassembly from valve body. Remove body gasket and core assembly with core spring.
2. For normal valve maintenance (cleaning and/or rebuilding) it is not necessary to remove the valve seat.
3. Unscrew valve end cap from valve body. For 3/4” NPT cast stainless steel valves, remove six bolts and lockwashers using a 1/2” wrench, then remove valve bonnet.
4. Remove end cap gasket or bonnet gasket (3/4” NPT stainless steel construction), piston spring and piston assembly. To remove piston assembly, a small hole is pro-vided through the wall of the piston assembly. Hook an appropriate tool or a bent piece of wire in hole and pull piston assembly from valve body.
5. All parts are now accessible to clean or replace. If parts are worn or damaged, install a complete ASCO Rebuild Kit. Parts included in the kit are marked with aster-isks in Figure 6-28 on page 68. Clean internal passage ways in valve body.
ASCO Series 8327
1. Unscrew solenoid base subassembly from valve body and remove solenoid base gasket.
2. Remove core spring from top of core/insert subassembly.
3. Pull core/insert subassembly from valve body cavity and remove insert gasket.
4. All parts are now accessible to clean or replace. If parts are worn or damaged, install a complete ASCO Rebuild Kit. Parts included in the kit are marked with aster-isks in Figure 6-29 on page 69.
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ASCO Series 8262
1. Unscrew solenoid base subassembly with bonnet washer attached.
2. Remove core assembly, plugnut gasket, plugnut assembly, stem, disc, disc spring solenoid base gasket and retainer.
NOTE: On valve catalog numbers with suffix “T” a Teflon plugnut retainer gasket will be pres-ent under the retainer.
3. All parts are now accessible to clean or replace. If parts are worn or damaged, install a complete ASCO Rebuild Kit. Parts included in the kit are marked with aster-isks in Figure 6-30 on page 70.
Valve Re-assembly
ASCO Series 8223
1. Lubricate all gaskets, piston ring, rider rings and piston and u-cups with an oxygen compatible lubricant (e.g., Castrol Braycote 601EF or Christo-Lube MCG). Apply only a thin film.
2. Assemble valve as shown in Figure 6-28. See Table ??? for required torque values. For 3/4” NPT cast stainless steel construction, hand thread screws into valve body and torque in a crisscross manner.
Table 6-2 ASCO Series 8223 Torque Values
PART NAME TORQUE [IN-LBS] TORQUE [NM]
Solenoid Base Subassembly 175 +/- 25 17.8 +/- 2.8
Valve Seat 45 +/- 5 5.1 +/- 0.6
End Cap 360 40.7
Bonnet Screws 144 +/- 15 16.3 +/- 1.7
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Figure 6-28: ASCO Series 8223 valve disassembly
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ASCO Series 8327
1. Lubricate all gaskets, piston ring, rider rings and piston and u-cups (shown in Fig-ure 6-29) with an oxygen compatible lubricant (e.g., Castrol Braycote 601EF or Christo-Lube MCG). Apply only a thin film.
Figure 6-29: ASCO Series 8327 valve disassembly
2. Snap insert gasket into the groove of the core/insert subassembly. Be sure to use the proper size gasket.
3. Install core/insert subassembly into body cavity and push it gently down until the gasket of the insert just seals in the cavity of the body.
4. Install core spring in top of core/insert subassembly. Close end of core spring pro-trudes from top of core.
5. Install solenoid base gasket and solenoid base subassembly. Torque solenoid base subassembly to 260 +/- 25 in-lbs [30 +/- 3 Nm]
ASCO Series 8262
1. Lubricate all gaskets, piston ring, rider rings and piston and u-cups with an oxygen compatible lubricant (e.g., Castrol Braycote 601EF or Christo-Lube MCG). Apply only a thin film.
2. Replace disc spring, disc, stem, (plugnut retainer gasket on suffix “T” valve con-structions only), solenoid base gasket and plugnut assembly.
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3. Install plugnut gasket, core (small end into solenoid base assembly) and solenoid base subassesmbly with bonnet washer. Torque solenoid base assembly to 175 +/- 25 in-lbs [19.830 +/- 2.8 Nm].
Figure 6-30: ASCO Series 8262 valve disassembly
Common Reassembly
1. Install solenoid into body. Install assembly in PEM Electrolyzer.
2. Connect tubing to valve according to the markings on valve body. When tighten-ing the tubing, do not use valve or solenoid as a lever. Locate wrenches applied to valve body or tubing as close as possible to connection point.
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WARNING: To prevent the possibility of death, serious injury or property damage, check valve for proper operation before returning to service. Also perform internal seat and external leakage tests with a nonhazardous, noncombustible fluid.
3. Restore line pressure and electrical power supply to valve.
4. After maintenance is completed, operate the valve a few times to be sure of proper operation. A metallic click indicates the solenoid is operating.
6.2.14 DI bed, Catalyst and Molecular Sieve Check and ReplacementThe DI bed is an ion exchange resin found inside DI filter FLT1005 that helps improve water purity (see P6070061). Feed water quality and hours of operation can affect the time it takes the bed to reach saturation. The recommended replacement cycle is 3000hrs of operation (or less if saturation of the bed is suspected). Saturation is gauged by the monitoring software water conductivity reading.
The catalyst is found in the Oxygen Removal Reactor (also called the Deoxo vessel, Fig-ure 6-31). The molecular sieve is found in the drying columns VSSL2014 and VSSL2015 (also called Dryers, Figure 6-32). Recommended replacement cycle is 4 years for both catalyst and molecular sieve.
Figure 6-32: Molecular Sieves VSSL2014 and VSSL 2015 (Dryers)
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
WARNING: Use of other than oxygen compatible lubricants on oxygen service lines is a serious hazard. Spontaneous combustion can occur. Ensure that your hands are clean and free of organic grease or lubricants when servicing oxygen lines. Do not use tools or equipment contaminated by orgainc grease or lubricants.
6.2.14.1Tools Required
Open wrench 5/16”, 7/16”, 9/16”, 11/16”, 7/8”
Funnel
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Drain pan
Shop cloth or paper towel
Ion exchange resin (P/N 1039136)
Catalyst (P/N 1011973)
Molecular sieve (P/N2003448)
Screen gasket (2pcs, P/N1039055)
¼” compression cap
Pressure gauge, 200psig
140 psig nitrogen supply
6.2.14.2Personal Protective Equipment
Safety glasses
Safety shoes
Dust mask
6.2.14.3DI Resin Bed Replacement
1. Switch power off and lock/tag out main disconnect. Cell stack must be completely depressurized and free from any residual electrical charge.
2. Remove unit back cover.
3. Begin by draining filter FLT1005. Remove the drain compression plug on the right side of the PEM Electrolyzer (if drain port plugged). Open drain hand valve HV5002 and collect water in a drain pan. Remove the filter vessel by undoing the compres-sion fittings and removing the securing cushion clamps.
4. Hold vessel in vertical position and undo/remove the top sanitary clamp (Figure 6-33).
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Figure 6-33: DI Bed Top Removal
5. Remove top screen gasket carefully (Figure 6-34). Remove bottom sanitary clamp and seal gasket only if it is suspected that the seal surface or screen are damaged. Screen gasket can be reused if in good condition, otherwise replace it.
Figure 6-34: DI Bed Screen Removal
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6. Empty the ion exchange resin and dispose of it in accordance with local environ-mental laws and regulations. Fill vessel with fresh resin while slightly tapping vessel to compact resin. Set the screen gasket in position. Ensure that sealing surface is clean and free of resin. Set and hand tighten the sanitary clamp, taking care not to overtighten it (Figure 6-35).
Figure 6-35: DI Bed Reassembly
7. Reinstall DI filter FLT1005, securing the cushion clamp(s) in place and reconnecting its fittings.
8. Set hand valves HV5001 HV 5002 and HV5003 for normal operation and plug the unit drain port if previously plugged (port is located on the outside bottom-left of the housing). Start unit and monitor for leaks. If any leaks are found, fix them according to Section 6.2.3 Gas/Water Leak Check on page 36.
6.2.14.4Catalyst and Molecular Sieve Replacement
1. Switch power off and lock/tag out main disconnect. Cell stack must be completely depressurized and free from any residual electrical charge.
2. Remove unit back cover.
3. Remove respective vessel(s) by undoing the compression fittings and removing the cushion clamps.
Important: Be careful not to break the heating coil ends at the bottom of oxygen removal reac-tor (Deoxo vessel) R2009.
4. Secure vessel in a bench vise and remove side plug. Empty vessels of old catalyst/molecular sieve. The vessel may be gently tapped with a hammer to help displace beads. Take care not to damage the heating coil located inside oxygen removal reactor (Deoxo vessel) R2009.
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5. Fill the vessel with fresh catalyst/molecular sieve using a funnel (Figure 6-36). Tap the vessel from time to time to help beads settle .
Figure 6-36: Molecular Sieve Refill
6. Reinstall the vessel side plug. Use only Teflon tape and oxygen compatible paste. Do not use any oxygen incompatible lubricant or sealant.
7. Leak test vessels before reinstalling by pressurizing with nitrogen at 140 psig.
8. Reinstall vessel in its original location. Reconnect process fittings and secure vessel with the cushion clamp(s).
9. Set hand valves HV5001, HV 5002 and HV5003 for normal operation and plug the unit drain port if previously plugged (port is located on the outside bottom-left of the housing). Start unit and monitor for leaks. If any leaks are found, fix them according to Section 6.2.3 Gas/Water Leak Check on page 36.
10. When all leaks are fixed, disconnect unit from power, lock out disconnect and tag. Allow cell stack to electrically discharge.
11. Reinstall back cover.
12. Run unit and set for automatic operation.
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6.3 Process Adjustment ProceduresThe dryer regeneration and shutdown depressurization metering valves, OR2017 and OR2018 respectively, are factory set. Unless it is suspected that the settings have altered, the following adjustment procedures do not need to performed.
6.3.1 Dryer Regeneration Flow Rate Check and AdjustmentDryer regeneration flow rate is factory set to meet dry regeneration requirements when unit runs at nominal production rate. Optionally, it can be set for lower production rates in accordance with customer needs. Typically the regeneration flow rate should be 20% of production volume. A regeneration flow rate lower than this number will lead over to poor dryer performance (humid gas) ; a flow rate that is too large will waste hydrogen gas and reduce the PEM Electrolyzer efficiency.
Adjustment of the regeneration flow rate is a complex tune up operation and should be done only by qualified personnel and only when absolutely necessary (e. g., if the pro-duction rate desired by customer differs significantly from the one for which the regen-eration flow rate was factory tuned).
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
6.3.1.1 Tools Required
Open wrench 9/16”
Precision hydrogen flow meter (0-30 L/min)
6.3.1.2 Personal Protective Equipment
Safety glasses
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Safety shoes
6.3.1.3 Regeneration Flow Rate Check
1. Shut down unit, lock/tag power out and isolate the PEM Electrolyzer from hydro-gen storage or user process by closing the respective isolation. Isolation valve must be locked out, closed and tagged.
2. Disconnect hydrogen to storage/user line and install the flow meter in place of it. Tube the flow meter outlet to the hydrogen vent. Make sure all fittings are swaged properly (Figure 6-37).
Figure 6-37: Hydrogen Flow Meter
3. Remove back cover of the unit and shut the regeneration flow completely off by closing metering valve OR2017 (Figure 6-38).
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Figure 6-38: Metering Valve OR2017
NOTE: Do not overtighten metering valve when closing. Overtightening will damage the valve.
4. Run unit and allow the flow meter reading to stabilize. With metering valve OR 2017 completely closed, adjust stack current to nominal value using the on board potentiometer (Figure 6-39). The hydrogen flow meter reading will show approxi-mately 125% of unit nominal production rate.
Figure 6-39: Stack Current Potentiometer
5. After the flow meter reading stabilizes, slowly open the metering valve OR2017 until the hydrogen meter reading drops to nominal hydrogen-to-user production
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rate. Now the dryer regeneration flow value is set for 20% of the cell stack hydro-gen output for the hydrogen production requested.
6. Shut down unit, allow time for depressurization and reconnect unit as per original configuration.
WARNING: A nitrogen purge of any hydrogen lines that have been exposed to air is required .
7. After N2 purge to applicable lines is complete, set unit for automatic operation and allow PEM Electrolyzer to run for at least 15 minutes.
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6.3.2 Shutdown Depressurization Rate Check and AdjustmentThe shutdown depressurization rate is factory set and sealed. Only adjust if factory set-point has been modified (accidentally or otherwise).
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar volt-age every 10 minutes until it has fallen to less than 1 Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
WARNING: Ensure the PEM Electrolyzers is depressurized before servicing.
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
6.3.2.1 Tools Required
Monitoring Software
Stopwatch
6.3.2.2 Personal Protective Equipment
Safety glasses
Safety shoes
6.3.2.3 Shutdown Depressurization Check
1. Turn unit off and remove back cover.
2. Locate metering valve OR2018 (Figure 6-40). Turn power on and make sure that monitoring software runs on line.
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PROCESS ADJUSTMENT PROCEDURES PEM ELECTROLYZER
Figure 6-40: Metering Valve OR2018
3. Bring unit to run mode and allow pressure to rise to normal operating level.
4. Simultaneously press PEM Electrolyzer stop button and start stopwatch.
5. Observe the system status on the monitoring software.
6. Stop the stopwatch when PEM Electrolyzer status changes from shutdown to stand by. Record time; it must be between 3min 30 sec and 4 min 30 sec.
NOTE: Do not overtighten metering valve when closing. Overtightening will damage the valve.
7. If the recorded time is less than 3 min 30 sec, turn the metering valve (OR2018) clockwise ¼ of a turn or less (closing it). Repeat steps 3 -6 as many times as neces-sary to increase the depressurization time to within range.
8. If the recorded time is greater than 4 min 30 sec, turn the metering valve (OR2018) counterclockwise ¼ of a turn or less (opening it). Repeat steps 3 -6 as many times as necessary to decrease the depressurization time to within range.
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7 | TroubleshootingThis section outlines the possible fault conditions that may be encountered while operating the equipment. It describes PEM Electrolyzer responses to faults, possible causes of faults and actions that should be taken to troubleshoot the fault and bring the PEM Electrolyzer back to normal operating conditions. If further assistance is required, contact Hydrogenics Corporation for technical support (see Section 1.3 Customer Assistance on page 2).
WARNING: Risk of severe burns. Do not attempt to service the PEM Electrolyzer while it is still operating. Ensure the unit has completely cooled to ambient temperature before servicing.
WARNING: Before removing covers or servicing, turn off the unit and then check bus bar voltage every 10 minutes until it has fallen to less than 1Vdc. Verify voltage across the load bus bars using a voltmeter or multimeter.
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FAULTS PEM ELECTROLYZER
7.1 FaultsTable 7-1 7-1lists the faults displayed on the HMI, possible causes, and actions to take to correct the fault.
Table 7-1: Fault Troubleshooting
FAULT MESSAGE ON SCREEN
TRIP POINT SENSOR VALID MODES CHECK
Internal Hydro-gen Level High
>40% LEL inside enclosure
GD1000 All Check for leaks, check detector (Section 6.2.3 Gas/Water Leak Check on page 36). In the event that a cell stack crossover leak is found, contact Hydrogenics (Section 1.3 Customer Assistance on page 2).
HWSS Over-Pres-sure
>130 psi PSH2100 All Check dryer BPR setting, O2 BPR setting, demand switch, hydrogen pres-sure transducer, PSH2100, SV2012, SV2013 and SV2023 (Section 6.2.13 Solenoid Valve Mainte-nance on page 62). Check filters and lines for possible blockage (Sec-tion 6.2.6 Oxygen and Hydrogen Filter Elements Replacement on page 42).
HWSS Over-Temprature
>90°C TSH2002
All Stack temperature sensor as it should have tripped first, check TSH2002, radi-ator fan, air inlet, ambient temp > 40oC
RT1100 Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check sensor and connec-tions
Stack Voltage Sensor Out of Range
Sensor output <0mA or >20mA
VM1500 Pressurize, H2 Purge, Run Check sensor and connec-tions
Stack Current Sensor Out of Range
Sensor ouput <0.3V or >4.7V
CM1500 Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check sensor and connec-tions
Air Flow Speed Sensor Out of Range
Sensor ouput <0.8V or >5.2V
AFS1000 Cabinet Purge, Fill Water, Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check sensor and connec-tions, confirm sensor alignment (Section 6.2.7 Air Flow Speed Sensor Check on page 45)
H2 Pressure Sen-sor Out of Range
Sensor output <2.4mA or >20mA
PT1100 Cabinet Purge, Fill Water, Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check sensor and connec-tions (Section 6.2.12 Pres-sure Transmitter Check on page 57)
O2 Pressure Sen-sor Out of Range
Sensor output <2.4mA or >20mA
PT1010 Cabinet Purge, Fill Water, Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check sensor and connec-tions (Section 6.2.12 Pres-sure Transmitter Check on page 57)
Stack Tempera-ture Sensor Out of Range
Sensor output <0V or >10V
TE1004 Cabinet Purge, Fill Water, Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check sensor and connec-tions
Reactor Temper-ature Sensor Out of Range
Sensor output <0V or >10V
TE1004 Cabinet Purge, Fill Water, Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check sensor and connec-tions
Table 7-1: Fault Troubleshooting
FAULT MESSAGE ON SCREEN
TRIP POINT SENSOR VALID MODES CHECK
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Fail to Prime Pump
More than 15 attempts to prime pump
PMP1003 & FSL1007
Prime Pump Check PMP1003, check FSL1007, drain O2 separa-tor (TK1002) and attempt restart of system. Change DI bed (Section 6.2.14.3 DI Resin Bed Replacement on page 73)
Fail to Polish Water
>5 minutes in pol-ish water state
RT1100 & FLT 1005
Polish Water Replace DI Resin in FLT1005 (Section 6.2.14.3 DI Resin Bed Replacement on page 73), check RT1100
Fail to Pressurize System
>15 minutes in pressurize state
PT1100 Pressurize Check PRV3004/PRV2007 setting, check SV3005 (should be closed), check DT2004 and DT3006 seals
External Detec-tor Fault
User supplied shutdown signal
-- All Check external shutdown signal source, check ter-minals 92 and 93 for 24V
Water Flow Switch Fault
False for > 5seconds
FSl1007 Polish Water, Pressurize, H2 Purge, Run
Check PMP1003, check FSL1007, drain O2 sepera-tor (TK1002) and attempt restart of system
DI Tank Level Switch Malfunc-tion
LSL1000 false &LSH1000 true
LSL1000 & LSH1000
Fill Water, Prime Pump, Pol-ish Water, Pressurize, H2 Purge, Run
Check LSL1000 & LSH1000, check for water in O2 sperator (TK1002)
Inlet Tank Level Switch Malfunc-tion
LSL4003 false & LSH4003 true
LSL4003 & LSH4003
Fill Water, Prime Pump, Pol-ish Water, Pressurize, H2 Purge, Run
Check LSL4003 & LSH4003, check for water in DI water tank (tk4007)
DI Water Level Low
False >1 minute LSL1000 Fill Water, Prime Pump, Pol-ish Water, Pressurize, H2 Purge, Run
Check PMP1000, SV1127, LSL1000, check for water in O2 seperator (TK1002)
Inlet Water Level Low
False >1 minute LSL4003 Fill Water, Prime Pump, Pol-ish Water, Pressurize, H2 Purge, Run
Check DI water supply is on, check for water in DI tank (TK4007), check SV4003 (Section 6.2.13 Solenoid Valve Mainte-nance on page 62)
Table 7-1: Fault Troubleshooting
FAULT MESSAGE ON SCREEN
TRIP POINT SENSOR VALID MODES CHECK
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Stack Over-Tem-prature
>80°C TE1004 Fill Water, Prime Pump, Pol-ish Water, Pressurize, H2 Purge, Run
Check FAHX1004 not blocked, check FAHX1004 fan (Section 6.2.4 Check/Clean Radiator and Venti-lation Fans on page 37), check TE1004
Stack Under-Temprature
<5°C TE1004 Fill Water, Prime Pump, Pol-ish Water, Pressurize, H2 Purge, Run
Check ambient tempera-ture, check TE1004
DeOxo Over-Temprature
>110°C TE2010 Run Check TE2010, possible O2 crossover in stack, contact Hydrogenics (Sec-tion 1.3 Customer Assis-tance on page 2)
DeOxo Under-Temprature
<5°C TE2010 Run Check ambient tempera-ture, check TE2010
Water Resistivity Under Limit
<2MOhm for >5minutes
RT1100 Pressurize, H2 Purge, Run Replace DI Resin in FLT1005 (Section 6.2.14.3 DI Resin Bed Replacement on page 73), check RT1100
Stack Over-Volt-age
>29V VM1500 All Check input voltage, check VM1500 (Section 6.2.11 Current Sensor CM1500 and Voltage Sen-sor VM1500 Check and Replacement on page 54)
Stack Under-Voltage
<18V VM1500 All Check input voltage, check VM1500 (Section 6.2.11 Current Sensor CM1500 and Voltage Sen-sor VM1500 Check and Replacement on page 54)
Wait for Stack Voltage Timeout
<18V for 10 sec VM1500 Pressurize Check CR517 & CR519
Table 7-1: Fault Troubleshooting
FAULT MESSAGE ON SCREEN
TRIP POINT SENSOR VALID MODES CHECK
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Stack Over-Cur-rent
>250A CM1500 Pressurize, H2 Purge, Run Check CM1500 (Section 6.2.11 Current Sensor CM1500 and Voltage Sen-sor VM1500 Check and Replacement on page 54), check for short circuit
Stack Under-Current
<20A CM1500 H2 Purge, Run Check CM1500 (Section 6.2.11 Current Sensor CM1500 and Voltage Sen-sor VM1500 Check and Replacement on page 54), raise input voltage, check for loose connection (Sec-tion 6.2.9 Cell Stack DC Cable Connection and Equipment Grounding/Bonding Check on page 51)
Air Flow Speed Under Limit
<0.5m/s for 1 min-ute
AFS1000 Cabinet Purge, Fill Water, Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check for blockages in ventilation holes, check FAV1000, AFS1000 (Sec-tion 6.2.7 Air Flow Speed Sensor Check on page 45)
H2 Over-Pres-sure
>120psi PT1100 Run Check PRV3004/PRV2007 setting (Section 6.2.8.3 PRV3004 Setpoint Adjust-ment on page 48), check PRV2023 setting, check PT1100 (Section 6.2.12 Pressure Transmitter Check on page 57). Check filters and lines for possible blockage (Section 6.2.6 Oxygen and Hydrogen Fil-ter Elements Replacement on page 42)
Table 7-1: Fault Troubleshooting
FAULT MESSAGE ON SCREEN
TRIP POINT SENSOR VALID MODES CHECK
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O2 Over-Pres-sure
>120psi PT1010 Run Check PRV3004 setting (Section 6.2.8.3 PRV3004 Setpoint Adjustment on page 48), check O2 vent for blockage, check PT1010 (Section 6.2.12 Pressure Transmitter Check on page 57). Check filters and lines for possible blockage (Section 6.2.6 Oxygen and Hydrogen Fil-ter Elements Replacement on page 42)
Differential Pres-sure High
>15psi PT1010 & PT1100
Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check PRV2023/2007 set-ting, check O2 vent for blockage, check PT1100 & PT1010 (Section 6.2.12 Pressure Transmitter Check on page 57). Check DT2004/DT3006 seat seals (Section 6.2.10 Drain Traps DT 2004 and DT3006 Check on page 52), check for leaks, open lines (Sec-tion 6.2.3 Gas/Water Leak Check on page 36)
Differential Pres-sure Low
<0.5psi PT1010 & PT1100
Run Check PRV3004/2007 set-ting (Section 6.2.8.3 PRV3004 Setpoint Adjust-ment on page 48), check for leaks, open lines, check non-return valve CHK2037, check DT2004/DT3006 seat seals (Sec-tion 6.2.10 Drain Traps DT 2004 and DT3006 Check on page 52)
Table 7-1: Fault Troubleshooting
FAULT MESSAGE ON SCREEN
TRIP POINT SENSOR VALID MODES CHECK
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FAULTS PEM ELECTROLYZER
H2 Under-Pres-sure
<50psi PT1100 Run Check DT2004 seat seals (Section 6.2.10 Drain Traps DT 2004 and DT3006 Check on page 52), PRV3004 setting (Section 6.2.8.3 PRV3004 Setpoint Adjustment on page 48), check PT1100 (Section 6.2.12 Pressure Transmit-ter Check on page 57), check for leaks (Section 6.2.3 Gas/Water Leak Check on page 36)
O2 Under-Pres-sure
<50psi PT1010 Run Check DT3006 seat seals (Section 6.2.10 Drain Traps DT 2004 and DT3006 Check on page 52), check PRV3004 setting, check PT1010 (Section 6.2.12 Pressure Transmitter Check on page 57), check for leaks (Section 6.2.3 Gas/Water Leak Check on page 36)
Loss of FCVM Heart Beat
No communica-tion for 5 seconds
FCVM Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check FCVM connections
Warning: Stuck Start Button
Start button true for > 1 minute
Prime Pump, Polish Water, Pressurize, H2 Purge, Run
Check start button and wiring
Warning: FCVM Cell Voltage Slope Over Limit
Shutdown
ESTOP (System Cannot Run) Call Hydrogen-ics for Assis-stance
Run Contact Hydrogenics Cus-tomer Service (Section 1.3 Customer Assistance on page 2)
Table 7-1: Fault Troubleshooting
FAULT MESSAGE ON SCREEN
TRIP POINT SENSOR VALID MODES CHECK
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INSTALLATION, OPERATION AND MAINTENANCE MANUAL TECHNICAL SUPPORT
7.2 Technical SupportWhen calling for support, the Hydrogenics’ technical support department may require the following information:
Ambient Temperature: Temperature outside the Charge Station enclosure, as mea-sured at any point on the surface of the Charge Station enclosure.
Anode: Electrically negative electrode at which water is split to form hydrogen.
Cathode: Electrically positive electrode at which water is split to form oxygen.
Cell: One complete repeating unit consisting of two bipolar plates, the diffusion/sup-port media, electrodes and the solid polymer membrane.
Charge Station Cell Stack: An assembly of single electrolyzer cells arranged in series.
E-stop: Emergency Stop.
ECU: Engine Control Unit. This is a microprocessor-based unit that supervises and con-trols all system functions for the Charge Station.
HMI: Human Machine Interface. The status display on the PEM Electrolyzer front panel.
kPa: Kilopascals (pressure), understood to be an absolute value unless specified other-wise.
LEL: Lower Explosive Limit.
LFL: Lower Flammability Limit.
MOC: Minimum Oxygen Concentration.
PPE: personal protective equipment, e.g. safety glasses.
psi, psia vs. psig: pounds per square inch (pressure); psia “absolute” (includes atmo-spheric pressure in measurement) vs. psig “gauge” (pressure internal to system only).
Relative Humidity: The measured partial pressure of the gas at the operating temper-ature process conditions divided by the theoretical partial pressure of the gas at the same temperature.
SI: International System of Units.
SLPM: standard litres per minute—see “Standard Conditions”.
Stack Operation: The stack is considered to be "operating" when the current is being drawn by the stack (main DC contactor is closed). This time will be recorded by the sys-tem’s hour meter HM1.
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PEM ELECTROLYZER
Standard Conditions: Hydrogenics’s conventions for determining a "standard litre" vary depending on the material being measured:
A standard litre of gas is referenced to 101.3 kPaabs at 0 °C (except for air).
A standard litre of ambient air is referenced to 101.3 kPaabs at 21 °C
A standard litre of water (or other liquid) is referenced to 101.3 kPaabs at 20 °C.
Vdc: Volts (direct current).
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Appendix B: CAN Specification
The CAN protocol is used for communication between the PEM Electrolyzer and moni-toring software. It consists of operational commands and status updates from the PEM Electrolyzer. The PEM Electrolyzer uses CAN 2.0 A (11 bit) Standard, with regular ID format and a Baud rate of 250 kbits/sec.
CAN 2.0 A is an ISO standard: ISO 11898/11519. Robert Bosch GmbH, the CAN spec developer, maintains a CAN information Web site at http://www.semiconduc-tors.bosch.de/en/20/can/.
NOTE: Data flow in CAN messages is from least to most significant bit. Multi-byte values are also ordered from least to most significant.
Table B-1 lists the main CAN IDs and their functions. Details of particular CAN ID bytes are provided in Section B.2 on page 4.
B.2 Byte Message DetailsDetails on CAN ID 100 byte 0, CAN ID 103 bytes 0-4 and CAN ID 200 bytes 0-7 are given below.
B.2.1 CAN ID 100
Table B-2: CAN ID 100 (Hex) Byte 0 Values
BIT MESSAGE
0x00 (0) -
0x01 (1) Init
0x02 (2) Standby
0x03 (3) Start Ready
0x04 (4) Cabinet Purge
0x05 (5) Fill Water
0x06 (6) Prime Pump
0x07 (7) Polish Water
0x08 (8) Pressurize System
0x09 (9) H2 Purge
0x0A (10) Run
0x0B (11) Temperature Recovery
0x0C (12) Shutdown
0x0D (13) Estop
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B.2.2 CAN ID 103
Table B-3: CAN ID 103 (Hex) Byte 0 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Internal Hydrogen Level High
0x02 (00000010) HWSS Over-Pressure Switch
0x04 (00000100) Inlet Tank Low Level Switch
0x08 (00001000) Inlet Tank High Level Switch
0x10 (00010000) DI Tank Low Level Switch
0x20 (00100000) DI Tank High Level Switch
0x40 (01000000) DI Water Flow Switch
0x80 (10000000) Demand Switch
Table B-4: CAN ID 103 (Hex) Byte 1 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Rectifier Fault
0x02 (00000010) HWSS Over-Temperature Switch
0x04 (00000100) External Detector Fault
0x08 (00001000) Estop Button
0x10 (00010000) Start Button
0x20 (00100000) Stop Button
0x40 (01000000) HWSS OK
0x80 (10000000) Reset Buttom
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Table B-5: CAN ID 103 (Hex) Byte 2 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) DI Water Cooling Fan (PWM)
0x02 (00000010) Rectifier Power
0x04 (00000100) Oxygen Vent Valve
0x08 (00001000) Hydrogen Supply valve
0x10 (00010000) Water Inlet Valve
0x20 (00100000) Enclosure Ventilation Fan
0x40 (01000000) Red LED
0x80 (10000000) Green LED
Table B-6: CAN ID 103 (Hex) Byte 3 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Hydrogen Cooling Fan
0x02 (00000010) DI Water Circulation Pump
0x04 (00000100) Sensor Enable
0x08 (00001000) Rectifier Enable
0x10 (00010000) System Enable
0x20 (00100000) Electrical Cabinet Ventilation Fan
0x40 (01000000) DI Water Feed Pump
0x80 (10000000) Dryer Input and Output Valves
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B.2.3 CAN ID 200
Table B-7: CAN ID 103 (Hex) Byte 4 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Dryer Regen A Valve
0x02 (00000010) Dryer Regen B Valve
0x04 (00000100) -
0x08 (00001000) -
0x10 (00010000) -
0x20 (00100000) -
0x40 (01000000) -
0x80 (10000000) -
Table B-8: CAN ID 200 (Hex) Byte 0 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Internal Hydrogen Level High
0x02 (00000010) HWSS Over-Pressure
0x04 (00000100) HWSS Over-Temperature
0x08 (00001000) Cathode De-Pressurizing Timeout
0x10 (00010000) Anode De-Pressurizing Timeout
0x20 (00100000) FCVM Cell Voltage Out of Limits
0x40 (01000000) FCVM Cell Voltage Offset Over Limit
0x80 (10000000) -
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Table B-9: CAN ID 200 (Hex) Byte 1 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Water Conductivity Sensor Out of Range
0x02 (00000010) Stack Voltage Sensor Out of Range
0x04 (00000100) Stack Current Sensor Out of Range
0x08 (00001000) Flow Speed Sensor Out of Range
0x10 (00010000) Cathode Pressure Sensor Out of Range
0x20 (00100000) Anode Pressure Sensor Out of Range
0x40 (01000000) Stack Temperature Sensor Out of Range
0x80 (10000000) Reactor Temperature Sensor Out of Range
Table B-10: CAN ID 200 (Hex) Byte 2 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Fail to Fill DI Water Tank
0x02 (00000010) Fail to Fill Inlet Water Tank
0x04 (00000100) Fail to Prime Pump
0x08 (00001000) Fail to Polish Water
0x10 (00010000) Fail to Pressurize System
0x20 (00100000) External Detector Fault
0x40 (01000000) Rectifier Fault
0x80 (10000000) Water Flow Switch Fault
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Table B-11: CAN ID 200 (Hex) Byte 3 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) DI Water Tank Level Switch Malfunction
0x02 (00000010) Inlet Water Tank Level Switch Malfunction
0x04 (00000100) DI Water Level Low
0x08 (00001000) Inlet Water Level Low
0x10 (00010000) Stack Over-Temperature
0x20 (00100000) Stack Under-Temperature
0x40 (01000000) Reactor Over-Temperature
0x80 (10000000) Reactor Under-Temperature
Table B-12: CAN ID 200 (Hex) Byte 4 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Water Resisitivity Under Limit
0x02 (00000010) Stack Over-Voltage
0x04 (00000100) Stack Under-Voltage
0x08 (00001000) Wait for Stack Voltage Timeout
0x10 (00010000) Stack Over-Current
0x20 (00100000) Stack Under-Current
0x40 (01000000) -
0x80 (10000000) Air Flow Speed Under Limit
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Table B-13: CAN ID 200 (Hex) Byte 5 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Cathode Over-Pressure
0x02 (00000010) Anode Over-Pressure
0x04 (00000100) Differential Pressure High
0x08 (00001000) Differential Pressure Low
0x10 (00010000) Cathode Under-Pressure
0x20 (00100000) Anode Under-Pressure
0x40 (01000000) -
0x80 (10000000) -
Table B-14: CAN ID 200 (Hex) Byte 6 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Loss of FCVM Heart Beat
0x02 (00000010) -
0x04 (00000100) -
0x08 (00001000) -
0x10 (00010000) -
0x20 (00100000) -
0x40 (01000000) -
0x80 (10000000) -
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Table B-15: CAN ID 200 (Hex) Byte 7 Values
BIT MESSAGE
0x00 (00000000) -
0x01 (00000001) Stuck Start Button
0x02 (00000010) FCVM Cell Voltage Slope Over Limit
0x04 (00000100) -
0x08 (00001000) -
0x10 (00010000) -
0x20 (00100000) -
0x40 (01000000) -
0x80 (10000000) -
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Revision 3 HYDROGENICS CORPORATION C-1
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Appendix C: Material Safety Data Sheets (MSDS)
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Safety Data Sheet Hydrogen
001A Version : 1.17 Date : 29/06/1999
1 IDENTIFICATION OF THE SUBSTANCE/PREPARATION AND OF THE COMPANY
MSDS Nr 067A
Product name Hydrogen
Chemical formula H2
Company identification see heading and/or footer
Emergency phone numbers see heading and/or footer
2 COMPOSITION/INFORMATION ON INGREDIENTS
Substance/Preparation Substance.
Components/Impurities Contains no other components or impurities which will influence the classification of the product.
CAS Nr 01333-74-0
EEC Nr (from EINECS) 215-605-7
3 HAZARDS IDENTIFICATION
Hazards identification Compressed gas Extremely flammable
4 FIRST AID MEASURES
Inhalation In high concentrations may cause asphyxiation. Symptoms may include loss of mobility/consciousness. Victim may not be aware of asphyxiation. Remove victim to uncontaminated area wearing self contained breathing apparatus. Keep victim warm and rested. Call a doctor. Apply artificial respiration if breathing stopped.
Ingestion Ingestion is not considered a potential route of exposure.
5 FIRE FIGHTING MEASURES
Specific hazards Exposure to fire may cause containers to rupture/explode.
Hazardous combustion products None
Suitable extinguishing media All known extinguishants can be used.
Specific methods If possible, stop flow of product. Move container away or cool with water from a protected position. Do not extinguish a leaking gas flame unless absolutely necessary. Spontaneous/explosive re-ignition may occur. Extinguish any other fire.
Special protective equipment for fire fighters In confined space use self-contained breathing apparatus.
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6 ACCIDENTAL RELEASE MEASURES
Personal precautions Wear self-contained breathing apparatus when entering area unless atmosphere is proved to be safe. Evacuate area. Ensure adequate air ventilation. Eliminate ignition sources.
Environmental precautions Try to stop release.
Clean up methods Ventilate area.
7 HANDLING AND STORAGE
Handling and storage Ensure equipment is adequately earthed. Suck back of water into the container must be prevented. Purge air from system before introducing gas. Do not allow backfeed into the container. Use only properly specified equipment which is suitable for this product, its supply pressure and temperature. Contact your gas supplier if in doubt. Keep away from ignition sources (including static discharges). Segregate from oxidant gases and other oxidants in store. Refer to supplier's container handling instructions. Keep container below 50°C in a well ventilated place.
8 EXPOSURE CONTROLS/PERSONAL PROTECTION
Personal protection Ensure adequate ventilation. Do not smoke while handling product.
9 PHYSICAL AND CHEMICAL PROPERTIES
Molecular weight 2
Melting point -259 °C
Boiling point -253 °C
Critical temperature -240 °C
Relative density, gas 0.07 (air=1)
Relative density, liquid 0.07 (water=1)
Vapour Pressure 20°C Not applicable.
Solubility mg/l water 1.6 mg/l
Appearance/Colour Colourless gas
Odour None
Autoignition temperature 560 °C
Flammability range 4-75 vol% in air.
Other data Burns with a colourless invisible flame.
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10 STABILITY AND REACTIVITY
Stability and reactivity Can form explosive mixture with air. May react violently with oxidants.
11 TOXICOLOGICAL INFORMATION
General No toxicological effects from this product.
12 ECOLOGICAL INFORMATION
General No known ecological damage caused by this product.
13 DISPOSAL CONSIDERATIONS
General Do not discharge into areas where there is a risk of forming an explosive mixture with air. Waste gas should be flared through a suitable burner with flash back arrestor. Do not discharge into any place where its accumulation could be dangerous. Contact supplier if guidance is required.
14 TRANSPORT INFORMATION
Proper shipping name Hydrogen, compressed
UN Nr 1049
Class/Div 2.1
ADR/RID Item Nr 2, 1°F
ADR/RID Hazard Nr 23
Labelling ADR Label 3: flammable gas
Other transport information Avoid transport on vehicles where the load space is not separated from the driver's compartment. Ensure vehicle driver is aware of the potential hazards of the load and knows what to do in the event of an accident or an emergency. Before transporting product containers ensure that they are firmly secured and: - cylinder valve is closed and not leaking - valve outlet cap nut or plug (where provided) is correctly fitted - valve protection device (where provided) is correctly fitted - there is adequate ventilation. - compliance with applicable regulations.
15 REGULATORY INFORMATION
Number in Annex I of Dir 67/548 001-001-00-9.
EC Classification F+;R12
-Symbols F+: Extremely flammable
-Risk phrases R12 Extremely flammable.
-Safety phrases S9 Keep container in well ventilated place. S16 Keep away from ignition sources - No smoking. S33 Take precautionary measures against static discharges.
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16 OTHER INFORMATION
Ensure all national/local regulations are observed. Ensure operators understand the flammability hazard. The hazard of asphyxiation is often overlooked and must be stressed during operator training. Before using this product in any new process or experiment, a thorough material compatibility and safety study should be carried out. Details given in this document are believed to be correct at the time of going to press. Whilst proper care has been taken in the preparation of this document, no liability for injury or damage resulting from its use can be accepted.
1/4
Safety Data Sheet Oxygen
097A Version : 2.01 Date : 29/06/1999
1 IDENTIFICATION OF THE SUBSTANCE/PREPARATION AND OF THE COMPANY
MSDS Nr 097A
Product name Oxygen
Chemical formula O2
Company identification see heading and/or footer
Emergency phone numbers see heading and/or footer
2 COMPOSITION/INFORMATION ON INGREDIENTS
Substance/Preparation Substance.
Components/Impurities Contains no other components or impurities which will influence the classification of the product.
CAS Nr 07782-44-7
EEC Nr (from EINECS) 231-956-9
3 HAZARDS IDENTIFICATION
Hazards identification Compressed gas Oxidant. Strongly supports combustion. May react violently with combustible materials.
4 FIRST AID MEASURES
Inhalation Continuous inhalation of concentrations higher than 75% may cause nausea, dizziness, respiratory difficulty and convulsion.
5 FIRE FIGHTING MEASURES
Specific hazards Supports combustion. Exposure to fire may cause containers to rupture/explode. Non flammable
Hazardous combustion products None
Suitable extinguishing media All known extinguishants can be used.
Specific methods If possible, stop flow of product. Move container away or cool with water from a protected position.
Special protective equipment for fire fighters None.
2/4
6 ACCIDENTAL RELEASE MEASURES
Personal precautions Evacuate area. Ensure adequate air ventilation. Eliminate ignition sources.
Environmental precautions Try to stop release. Prevent from entering sewers, basements and workpits, or any place where its accumulation can be dangerous.
Clean up methods Ventilate area.
7 HANDLING AND STORAGE
Handling and storage Use no oil or grease. Open valve slowly to avoid pressure shock. Segregate from flammable gases and other flammable materials in store. Suck back of water into the container must be prevented. Do not allow backfeed into the container. Use only properly specified equipment which is suitable for this product, its supply pressure and temperature. Contact your gas supplier if in doubt. Keep away from ignition sources (including static discharges). Refer to supplier's container handling instructions. Keep container below 50°C in a well ventilated place.
8 EXPOSURE CONTROLS/PERSONAL PROTECTION
Personal protection Do not smoke while handling product. Wear suitable hand, body and head protection. Wear goggles with suitable filter lenses when use is cutting/welding. Avoid oxygen rich (>21%) atmospheres. Ensure adequate ventilation.
9 PHYSICAL AND CHEMICAL PROPERTIES
Molecular weight 32
Melting point -219 °C
Boiling point -183 °C
Critical temperature -118 °C
Relative density, gas 1.1 (air=1)
Relative density, liquid 1.1 (water=1)
Vapour Pressure 20°C Not applicable.
Solubility mg/l water 39 mg/l
Appearance/Colour Colourless gas
Odour No odour warning properties.
Autoignition temperature Not applicable
3/4
Flammability range Oxidiser.
Other data Gas/vapour heavier than air. May accumulate in confined spaces, particularly at or below ground level.
10 STABILITY AND REACTIVITY
Stability and reactivity May react violently with combustible materials May react violently with reducing agents. Violently oxidises organic material.
11 TOXICOLOGICAL INFORMATION
General No toxicological effects from this product.
12 ECOLOGICAL INFORMATION
General No ecological damage caused by this product.
13 DISPOSAL CONSIDERATIONS
General To atmosphere in a well ventilated place. Do not discharge into any place where its accumulation could be dangerous. Contact supplier if guidance is required.
14 TRANSPORT INFORMATION
Proper shipping name Oxygen, compressed
UN Nr 1072
Class/Div 2.2
Subsidiary risk 5.1
ADR/RID Item Nr 2,1° O
ADR/RID Hazard Nr 25
Labelling ADR Label 2: non flammable non toxic gas Label 05: fire intensifying risk.
Other transport information Avoid transport on vehicles where the load space is not separated from the driver's compartment. Ensure vehicle driver is aware of the potential hazards of the load and knows what to do in the event of an accident or an emergency. Before transporting product containers ensure that they are firmly secured and: - cylinder valve is closed and not leaking - valve outlet cap nut or plug (where provided) is correctly fitted - valve protection device (where provided) is correctly fitted - there is adequate ventilation. - compliance with applicable regulations.
4/4
15 REGULATORY INFORMATION
Number in Annex I of Dir 67/548 008-001-00-8.
EC Classification O;R8
-Symbols O: Oxidising
-Risk phrases R8 Contact with combustible material may cause fire.
-Safety phrases S17 Keep away from combustible material.
16 OTHER INFORMATION
Ensure all national/local regulations are observed. Ensure operators understand the hazard of oxygen enrichment. Before using this product in any new process or experiment, a thorough material compatibility and safety study should be carried out. Details given in this document are believed to be correct at the time of going to press. Whilst proper care has been taken in the preparation of this document, no liability for injury or damage resulting from its use can be accepted.
CONDITIONS UNDER WHICH PRODUCT IS CHEMICALLY UNSTABLE: At temperatures above 204°C decomposition occurs. Explosive reactions can occur in the presence of strong oxidizing agents such as concentrated nitric acid.
INCOMPATIBILITY (MATERIALS TO AVOID): Strong oxidizing agents such as nitric acid
HAZARDOUS DECOMPOSITION OR BY PRODUCTS: Carbon monoxide, carbon dioxide,
styrene, divinylbenzene, alkylamines, oxides of nitrogen, sulfur oxides and hydrochloric acid.
HAZARDOUS POLYMERIZATION: None
SECTION VI – HEALTH HAZARD DATA
NFPA HEALTH HAZARD: 1, Slight ROUTE OF ENTRY: Eye contact
EFFECT OF ACUTE EXPOSURE TO PRODUCT: Can produce mechanical irritation to the eyes.
May cause skin irritation of hypersensitive personnel.
EFFECT OF CHRONIC EXPOSURE TO PRODUCT: Mechanical irritation to the eyes and skin
SYMPTOMS OF EXPOSURE: Red, irritated eyes, itching and feeling that a particle exists
between the eyelid and eye.
EMERGENCY AND FIRST AID PROCEDURES: Flush eyes and skin with copious quantities of
water for 15 minutes. If irritation persists, see a physician.
TOXICITY DATA FOR A COMPOSITIONALLY SIMILAR MATERIAL IS: Not available
SECTION VII – PRECAUTIONS FOR SAFE HANDLING AND USE
STORAGE REQUIREMENTS: Avoid freezing or prolonged storage above 50°C because product contains water which could freeze or dry-out causing physical damage to the product.
SPECIAL SHIPPING INFORMATION: Avoid freezing or drying out.
IN CASE OF SPILL OR LEAK: Sweep area of product, collecting in a container for disposal.
WASTE DISPOSAL METHOD: As supplied, new or unused ion exchange resins are not
hazardous and therefore are not considered as hazardous waste. They may be disposed of
as ordinary trash according to local, state/provincial and federal regulations. Used resins
may meet the regulatory definition of hazardous wastes as a result of their service.
A representative sample of the material may be analyzed by a certified laboratory
following procedures set forth in 40 CFR261, APPENDIX II, METHOD 1311 TOXICITY
CHARACTERISTIC LEACHING PROCEDURE (TCLP) AND EP TOXICITY TEST PROCEDURE.
Based on the results obtained from these analyses, disposal of used resin can be
accomplished in accordance with applicable federal, state/provincial and municipal
regulations.
Avoid packing in glass columns. Product can expand and shatter the glass.
PERSONAL PROTECTIVE EQUIPMENT: Wear impervious gloves and splash goggles while handling
ion exchange material.
OTHER PROTECTIVE CLOTHING OR EQUIPMENT: Long sleeve shirts and long pants are
recommended to prevent skin contact.
WORK/HYGIENIC PRACTICES: Flush product from hands with soapy water. Care should be taken
to avoid contact with eyes until hands have been completely cleaned. Product has a tendency to
cling to skin. Care must be exercised to remove all product from skin. Sweep up spilled material
and transfer for proper disposal as spilled product causes area to become extremely slippery and
can cause falls.
SECTION IX – REGULATORY INFORMATION & REFERENCES
SARA TITLE III REPORTING REQUIREMENTS
SECTION 302 REPORTING IF ABOVE: None
SECTION 304 REPORTING IF ABOVE: None
SECTION 313 REPORTING REQUIRED: No
CERCLA REPORTING REQUIRED IF ABOVE: None
RCRA REPORTING REQUIRED: No
Product is not WHMIS controlled in Canada and does not have a WHMIS classification.
Product is considered non-hazardous under the OSHA hazard communication standard.
(29CFR1910.1200)
D.O.T. HAZARD NAME: Not regulated by D.O.T.
TDG CLASSIFICATION: Not regulated
REFERENCES
The data and recommendations presented herein are based upon our research and the
research of others and are believed to be accurate. However, no warranty is expressed or
implied regarding the accuracy of these data or the results to be obtained from the use
thereof.
Aldex Chemical Co. Ltd. assumes no responsibility for injury to customers or third persons
caused by the material if reasonable safety procedures are not adhered to as stipulated in
the data sheet. Additionally, since actual use by others is beyond our control, no guarantee,
expressed or implied, is made by Aldex Chemical Co. Ltd. as to the effects of such use,
the results to be obtained, or the safety and toxicity of the product nor does Aldex
Chemical Co. Ltd. assume any liability arising out of use, misuse, by others, of the product
referred to herein.
Information provided herein is provided by Aldex Chemical Co. Ltd. solely for customer’s
assistance in complying with the Occupational Safety and Health Acts and regulations
thereunder. Any other use is prohibited.
MATERIAL SAFETY DATA SHEET
SNOOP® January 2009
Page 1 of 4
1. PRODUCT IDENTIFICATION SNOOP®: Liquid leak detector for use on external surfaces only. Optimum usage temperatures are between 27°F and 200°F (-3°C and 93°C). Manufactured by: Emergency Contact: Swagelok Manufacturing Company Chemtrec (800) 424-9300 29495 F.A. Lennon Dr. Solon, Ohio 44139 Tel: (440) 349-5600 2. INGREDIENTS
Ingredients CAS # WT% PEL Water 7732-18-5 >95 Not Available
Surfactant Not Available <5 Not Available 3. HEALTH HAZARD INFORMATION • European Community Danger Group............... None. • Special Hazards for man or environment ........ None. • LC50/LD50 ......................................................... Not available.
No No Yes No Yes 4. FIRST AID MEASURES • If inhaled (Overexposure): Unlikely to be inhaled. • After contact with skin (Overexposure): Wash thoroughly with soap and water. If severe irritation
develops, seek medical attention. • After contact with eyes: Rinse thoroughly with water for 15 minutes, seek medical attention. Do not rub eyes. • If swallowed: Unlikely to cause illness, seek medical attention if needed. • Medical information: None known.
MATERIAL SAFETY DATA SHEET
SNOOP® January 2009
Page 2 of 4
5. FIRE FIGHTING MEASURES • Suitable extinguishing agents: Not applicable. • Unsuitable extinguishing agents: None known. • Special dangers caused by substance None known.
or preparation itself, by combustion products, or gases formed:
• Additional information: None.
Autoignition UEL LEL Sensitivities Not Applicable Not Applicable Not Applicable Not Available
6. ACCIDENTAL RELEASE MEASURES • Measures for protection of people: Eye and hand protection as needed to minimize excessive exposure. • Measures for protection of the
environment: None required. • Cleaning measures: Use absorbent material to clean spills. • Additional information: None. 7. HANDLING AND STORAGE • Safety information: None. • Information on protection from fire
or explosion: None. • Additional information: Store in a cool, dry place for optimal product performance. 8. EXPOSURE CONTROLS AND PERSONAL PROTECTION • Precautionary measures to protect
employees: None required. • Respiratory protection: None required. • Hand protection: Rubber gloves are recommended to minimize exposure. • Eye protection: Goggles are recommended when SNOOP® could splash in eyes. • Skin protection: Wash hands after use.
9. PHYSICAL AND CHEMICAL PROPERTIES
Appearance Odor pH Density Vapor Pressure Colorless liquid Neutral 6.75 +/- 0.75 1.0 gm/cm3 Not Available Boiling Point Melting Point Flash Point Flammability Explosive
212°F/100°C Not Available Not Available Not Available Not Available
MATERIAL SAFETY DATA SHEET
SNOOP® January 2009
Page 3 of 4
10. STABILITY AND REACTIVITY • Conditions to avoid: None. • Materials to avoid: Strong oxidizers, alkali metals, and compounds that react exothermically with water. • Hazardous decomposition products: None. 11. TOXICOLOGICAL INFORMATION • Acute toxic properties: None known. • Health effects: None known. • Additional health effects: None known.
Sensitization
Teratogenicity
Reproductive Toxicity
Mutagenicity
Synergistic Products
Carcinogenicity
Not Available Not Available Not Available Not Available Not Available Listed ingredients are not suspected
carcinogens according to NTP, IARC, and OSHA
12. ECOLOGICAL INFORMATION • Mobility: Comparable to water. • Degradability: Not established. • Accumulation: No adverse bioaccumulation or biomagnification effects known. • Short/Long term effects
on ecotoxicity: No known ecological affects. 13. DISPOSAL CONSIDERATIONS • Appropriate methods of disposal: Unused product not considered a hazardous waste in the United States. Dispose of in a responsible manner. • European Community (EC) considerations: Use appropriate waste codes based on ingredients. 14. TRANSPORT INFORMATION • Transport precautions: Consult applicable regulations when transporting this product. • Additional information: None.
MATERIAL SAFETY DATA SHEET
SNOOP® January 2009
Page 4 of 4
15. REGULATORY INFORMATION • US/Canadian regulation listing: SARA 313 - NO, Canada’s Controlled Products - NO, TSCA - YES • EC Relevant risk: None. • EC Relevant safety: S: 37/39 - Wear suitable gloves and eye/face protection.
S: 20 - When using do not eat or drink. • Additional information: Consult country codes for specific requirements. 16. OTHER INFORMATION • For further information contact: Your Swagelok Distributor or the contacts listed in Section 1 of this sheet. • Sources of information used Properties of individual ingredients were used to compile this document.
to compile document: This Material Safety Data Sheet was designed to give the distributors and users of SNOOP® information to handle and use the product in a responsible manner.
Preparation Data
Environmental and Safety Department (440) 248-4600 January 2009
Fire Extinguisher Type: Any means suitable for extinguishing surrounding fire
Fire Fighting Procedure: Wear self-contained breathing apparatus and protective clothing to prevent contact with skin and clothing.
Fire / Explosion Hazards:None Known.
SECTION 6 ACCIDENTAL RELEASE MEASURES
This material is non hazardous, wipe up and dispose of down drain.
Non-Hazardous Material. Clean up of Spills Requires no Special
Generally not hazardous in normal handling, Store away from water reactive materials.
Generally not hazardous in normal handling, Store away from water reactive materials.
Water, Deionized ASTM Type II 100% V/VCAS# 7732-18-5 None Established
Deionized Water
Equipment or Procedures.
SECTION 8 EXPOSURE CONTROLS/PERSONAL PROTECTION
Respiratory Protection: None required
Mechanical
Local ExhaustVentilation
Protective Gloves: None required
Eye Protection: None required
Other Protective Equipment: None required.
Store in a cool dry place. This Material is not considered hazardous. Store away from water reactive material.
SECTION 7 HANDLING AND STORAGE
SECTION 9 PHYSICAL AND CHEMICAL PROPERTIES
Melting Point: 0°C
Boiling Point: 100°C
Vapor Pressure: Information
not available
Vapor Density: Information
not available
Solubility in Water: Soluble
Appearance /Odors: Colorless
odorless liquid
Flash Point: Not flammable
Specific Gravity: 1
Percent Volatile by Volume: >99
Evaporation Rate 1
Auto Ignition Temp Not applicable
Lower Flamm. Limit in Air Not applicable
Upper Flamm. Limit in Air Not applicable
Evaporation Standard Water =1
SECTION 10 STABILITY AND REACTIVITY INFORMATION
Stability: Stable
Conditions to Avoid: Temperature extremes
Materials to Avoid: Strong Acids, Bases. Water reactive materials
Hazardous DecompositionProducts:
Not known to occur
Hazardous polymerization: Will Not Occur
Conditions to Avoid: None known
SECTION 11 Toxicological Information
SECTION 12 Ecological Information
SECTION 13 Disposal Considerations
Carcinogenic References: NTP Carcinogen - Known: No, IARC Category- None
Not Applicable.
Whatever cannot be saved for recovery or recycling should be flushed to sewer. If material
Page 2 of 4
Deionized Water
SECTION 14 Transport Information
SECTION 15 Regulatory Information
SECTION 16 Additional Information
becomes contaminated during use, dispose of accordingly. Dispose of container and unusedcontents in accordance with federal, state and local requirements.
Chemical Inventory Status –Part 1:Ingrdient Water (7732-18-5) TSCA Yes EC Yes Japan YES Australia Yes
Chemical Inventory Status –Part 2:Ingredient Water (7732-18-5)Korea Yes DSL Yes NDSL No Phil. Yes
Federal, State & International Regulations –Part 1: Ingredient.Water (7732-18-5) RQ No TPQ No List NO Chemical Catg No
Federal, State &International Regulations –Part 2:Ingredient Water (7732-18-5)CERCLA No 261.33 No 8(d) No
Chemical Weapons Convention: NoTSCA 12 (b):NoCDTA:No PURE/LIQUIDSARA 311/312: Acute: NoChronic: No Fire: NoPressure: No Reactivity: NoAustralian Hazchem Code: None allocatedPoison Schedule: None allocated
Conditions aggravated/Target organs: None known
DOT Classification: Not Regulated
DOT Regulations may change from time to time. Please consult the most recent D.O.T. regulations.
Page 3 of 4
Deionized Water
The information herein is believed to be accurate and is offered in good faith for the user's consideration and investigation. No warranty either expressed or implied is made for the completeness or accuracy of the information whether originating from the above mentioned company or not. Users of this material should satisfy themselves by independent investigation of current scientific and medical knowledge that the material can be used safely.
Health Reactivity
Flammability
NFPARevisions
0.17/30/2010 updated msds to 16 section from 10 section msds. STN
0
Page 4 of 4
Page 1/5
Material Safety Data SheetAccording to OSHA and ANSI
Printing date 05/31/2011 Reviewed on 09/28/2010
DR
1 Identification of the substance/mixture and of the company/undertaking
Product identifier
Product name: Molecular sieves, 5A
Stock number: 87955CAS Number:69912-79-4Relevant identified uses of the substance or mixture and uses advised against.Sector of Use SU24 Scientific research and development
Details of the supplier of the safety data sheetManufacturer/Supplier:Alfa Aesar, A Johnson Matthey CompanyJohnson Matthey Catalog Company, Inc.30 Bond StreetWard Hill, MA 01835-8099Tel: 800-343-0660Fax: 800-322-4757Email: [email protected]
Information Department: Health, Safety and Environmental DepartmentEmergency telephone number:During normal hours the Health, Safety and Environmental Department at (800) 343-0660. Afternormal hours call Carechem 24 at (866) 928-0789.
2 Hazards identification
Classification of the substance or mixtureThe substance is not classified according to the Globally Harmonized System (GHS).
Classification according to Directive 67/548/EEC or Directive 1999/45/EC Not applicableInformation concerning particular hazards for human and environment: Not applicable
Label elements
Labelling according to EU guidelines:Observe the general safety regulations when handling chemicalsClassification systemHMIS ratings (scale 0-4)(Hazardous Materials Identification System)
HEALTH
FIRE
REACTIVITY
0
0
0
Health (acute effects) = 0Flammability = 0Reactivity = 0
Other hazardsResults of PBT and vPvB assessmentPBT: Not applicable.vPvB: Not applicable.
3 Composition/information on ingredients
Chemical characterization: Substances(CAS#) Description:Molecular sieves (CAS# 69912-79-4)
4 First aid measures
Description of first aid measuresAfter inhalationSupply fresh air. If required, provide artificial respiration. Keep patient warm.Seek immediate medical advice.After skin contactImmediately wash with water and soap and rinse thoroughly.Seek immediate medical advice.After eye contactRinse opened eye for several minutes under running water. Then consult a doctor.After swallowing Seek medical treatment.
5 Firefighting measures
Extinguishing mediaSuitable extinguishing agentsProduct is not flammable. Use fire fighting measures that suit the surrounding fire.
(Contd. on page 2) USA
Page 2/5
Material Safety Data SheetAccording to OSHA and ANSI
Printing date 05/31/2011 Reviewed on 09/28/2010
Product name: Molecular sieves, 5A
(Contd. of page 1)
DR
Special hazards arising from the substance or mixtureIn case of fire, the following can be released:Metal oxide fumeSilicon oxideSodium oxideAdvice for firefightersProtective equipment:Wear self-contained respirator.Wear fully protective impervious suit.
6 Accidental release measures
Personal precautions, protective equipment and emergency proceduresWear protective equipment. Keep unprotected persons away.Ensure adequate ventilationEnvironmental precautions:Do not allow material to be released to the environment without proper governmental permits.Methods and material for containment and cleaning up: Pick up mechanically.Reference to other sectionsSee Section 7 for information on safe handlingSee Section 8 for information on personal protection equipment.See Section 13 for disposal information.
7 Handling and storage
HandlingPrecautions for safe handlingKeep container tightly sealed.Store in cool, dry place in tightly closed containers.No special precautions are necessary if used correctly.Information about protection against explosions and fires: The product is not flammable
Conditions for safe storage, including any incompatibilitiesStorageRequirements to be met by storerooms and receptacles: No special requirements.Information about storage in one common storage facility:Store away from water/moisture.Do not store together with oxidizing and acidic materials.Further information about storage conditions:This product is hygroscopic.Keep container tightly sealed.Store in cool, dry conditions in well sealed containers.Protect from humidity and water.
8 Exposure controls/personal protection
Additional information about design of technical systems:Properly operating chemical fume hood designed for hazardous chemicals and having an averageface velocity of at least 100 feet per minute.
Control parametersComponents with limit values that require monitoring at the workplace: Not required.Additional information: No data
Exposure controlsPersonal protective equipmentGeneral protective and hygienic measuresThe usual precautionary measures for handling chemicals should be followed.Keep away from foodstuffs, beverages and feed.Remove all soiled and contaminated clothing immediately.Wash hands before breaks and at the end of work.Breathing equipment: Use suitable respirator when high concentrations are present.Protection of hands:Impervious glovesCheck protective gloves prior to each use for their proper condition.Material of glovesThe selection of suitable gloves not only depends on the material, but also on quality.Quality will vary from manufacturer to manufacturer.Eye protection: Safety glassesBody protection: Protective work clothing.
USA(Contd. on page 3)
Page 3/5
Material Safety Data SheetAccording to OSHA and ANSI
Printing date 05/31/2011 Reviewed on 09/28/2010
Product name: Molecular sieves, 5A
(Contd. of page 2)
DR
9 Physical and chemical properties
Information on basic physical and chemical propertiesGeneral InformationAppearance:
Form: PelletsColor: Light brown
Odor: Not determinedOdour threshold: Not determined.
pH-value: Not applicable.
Change in conditionMelting point/Melting range: Not determinedBoiling point/Boiling range: Not determinedSublimation temperature / start: Not determined
Flammability (solid, gaseous) Not determined.
Ignition temperature: Not determined
Decomposition temperature: Not determined
Auto igniting: Not determined.
Danger of explosion: Product does not present an explosion hazard.
Explosion limits:Lower: Not determinedUpper: Not determined
Vapor pressure: Not applicable.
Density: Not determinedRelative density Not determined.Vapour density Not applicable.Evaporation rate Not applicable.
Solubility in / Miscibility withWater: Insoluble
Segregation coefficient (n-octonol/water): Not determined.
Viscosity:dynamic: Not applicable.kinematic: Not applicable.
Other information No further relevant information available.
10 Stability and reactivity
ReactivityChemical stabilityThermal decomposition / conditions to be avoided:Decomposition will not occur if used and stored according to specifications.Possibility of hazardous reactions No dangerous reactions knownIncompatible materials:Water/moistureAcidsOxidizing agentsHazardous decomposition products:Metal oxide fumeSilicon oxideSodium oxide
11 Toxicological information
Information on toxicological effectsAcute toxicity:Primary irritant effect:on the skin: May cause irritationon the eye: May cause irritationSensitization: No sensitizing effects known.Subacute to chronic toxicity:The toxicity of calcium compounds is generally due to the anion.The toxicity of sodium compounds is generally due to the anion.Inorganic silicon compounds may be acute inhalation irritants. Prolonged inhalation maycause pulmonary fibrosis known as silicosis.
(Contd. on page 4) USA
Page 4/5
Material Safety Data SheetAccording to OSHA and ANSI
Printing date 05/31/2011 Reviewed on 09/28/2010
Product name: Molecular sieves, 5A
(Contd. of page 3)
DR
Subacute to chronic toxicity:Aluminum may be implicated in Alzheimers disease. Inhalation of aluminum containing dustsmay cause pulmonary disease.Additional toxicological information:To the best of our knowledge the acute and chronic toxicity of this substance is not fullyknown.No classification data on carcinogenic properties of this material is available from the EPA,IARC, NTP, OSHA or ACGIH.
12 Ecological information
ToxicityAcquatic toxicity: No further relevant information available.Persistence and degradability No further relevant information available.Behavior in environmental systems:Bioaccumulative potential No further relevant information available.Mobility in soil No further relevant information available.Additional ecological information:General notes:Do not allow material to be released to the environment without proper governmental permits.Results of PBT and vPvB assessmentPBT: Not applicable.vPvB: Not applicable.Other adverse effects No further relevant information available.
13 Disposal considerations
Waste treatment methodsRecommendation Consult state, local or national regulations to ensure proper disposal.
Uncleaned packagings:Recommendation: Disposal must be made according to official regulations.
14 Transport informationNot a hazardous material for transportation.
DOT regulations:Hazard class: None
Land transport ADR/RID (cross-border)ADR/RID class: None
Maritime transport IMDG:IMDG Class: NoneMarine pollutant: No
Air transport ICAO-TI and IATA-DGR:ICAO/IATA Class: None
Special precautions for user Not applicable.
Transport/Additional information: Not dangerous according to the above specifications.Transport in bulk according to Annex II of MARPOL73/78 and the IBC Code Not applicable.
15 Regulatory information
Safety, health and environmental regulations/legislation specific for the substance ormixture
Product related hazard informations:Observe the general safety regulations when handling chemicals
National regulationsThis product is not listed in the U.S. Environmental Protection Agency Toxic SubstancesControl Act Chemical Substance Inventory. Use of this product is restricted to research anddevelopment only.Some or all of the components of this product are not listed on the Canadian DomesticSubstances List (DSL) or the Canadian Non-Domestic Substances List (NDSL).
Information about limitation of use: For use only by technically qualified individuals.Chemical safety assessment: A Chemical Safety Assessment has not been carried out.
USA(Contd. on page 5)
Page 5/5
Material Safety Data SheetAccording to OSHA and ANSI
Printing date 05/31/2011 Reviewed on 09/28/2010
Product name: Molecular sieves, 5A
(Contd. of page 4)
DR
16 Other informationEmployers should use this information only as a supplement to other information gathered bythem, and should make independent judgement of suitability of this information to ensureproper use and protect the health and safety of employees. This information is furnishedwithout warranty, and any use of the product not in conformance with this Material SafetyData Sheet, or in combination with any other product or process, is the responsibility of theuser.
Department issuing MSDS: Health, Safety and Environmental Department.Contact:Zachariah C. HoltGlobal EHS ManagerAbbreviations and acronyms:ADR: Accord européen sur le transport des marchandises dangereuses par Route (European Agreement concerning the InternationalCarriage of Dangerous Goods by Road)RID: Règlement international concernant le transport des marchandises dangereuses par chemin de fer (Regulations Concerningthe International Transport of Dangerous Goods by Rail)IMDG: International Maritime Code for Dangerous GoodsDOT: US Department of TransportationIATA: International Air Transport AssociationIATA-DGR: Dangerous Goods Regulations by the "International Air Transport Association" (IATA)ICAO: International Civil Aviation OrganizationICAO-TI: Technical Instructions by the "International Civil Aviation Organization" (ICAO)CAS: Chemical Abstracts Service (division of the American Chemical Society)HMIS: Hazardous Materials Identification System (USA)
USA
C- 2 HYDROGENICS CORPORATION Revision 3
INSTALLATION, OPERATION AND MAINTENANCE MANUAL PEM ELECTROLYZER
Revision 3 HYDROGENICS CORPORATION D-1
INSTALLATION, OPERATION AND MAINTENANCE MANUAL
Appendix D: P&ID
Revision 3 HYDROGENICS CORPORATION E-1
INSTALLATION, OPERATION AND MAINTENANCE MANUAL
Appendix E: Electrical Schematics
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REFERENCES
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
"If any of the original wire as supplied with the electrolyzer power system must be replaced , it must be replaced with wiring material having equivalent ratings with respect to ampacity, voltage and temperature."
WARNING !
ORANGE
RED
BLACK
BROWN
GREEN
BLUE
WIRE CODE DESIGNATION
VIOLET
GRAY
WIRE COLOUR
BRN
YELLOW
WHITE WHT
GRY
VIO
BLU
GRN
YEL
ORG
RED
BLK
DESIGNATION SPECIFIED
201 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
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Page:3
POWER
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
0-(23.8-28.3)V DC ;230A
CUSTOMERPOWER SUPPLY
TO VOLTAGE MONITOR DEVICE
CONN: 6321 ANDERSON
2
CM1500CURRENT SENSOR
01 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
1 GGND CONNECTOR
U334
14CELLS;28V; 216A
ELECTROLYZER STACK
-
+
4AW
GG
RN
/YEL
3/0
L1 3/0
L2
1
2CR517
/5/517
+P1 -P1
14AWGWHT/BLU3091
14AWGBLU3081
18AWGBLU3262
18AWGBLU3282
4/0
3081
4/0
3091
1
2CR519
/5/519
3/0
3083
3/0
3093
1 2
3 4
0.5AATDR0.5
FU326
2
1
FU320250A
CNN 250FERRAZ SHAWMUT
2
1
FU321250A
CNN 250FERRAZ SHAWMUT
18AWGBLU3261
18AWGBLU3281
BLU
14
AWG
3211
WH
T/BL
U 1
4 AW
G32
21
BLU
14
AWG
3211
0
1L1
2T1
3L2
4T2
5L3
6T3
DS30763A/24VDC
NON-FUSIBILE DISC. SWITCH
OT63FT3SABB
4/0
3082
4/0
3092
PS14/403
PS24/403
DC+ / 9/913
DC- / 9/914
L1 + L2- G
401
402
403
404
405
406
407
408
409
410
411
412
413
414
415
416
417
418
419
420
421
422
423
424
425
426
427
428
429
430
431
432
433
434
435
436
437
438
439
440
JASON LEMOS Next page:Page Group:Previous page:
1735
Page:4
24V/12V POWER SUPPLY
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
OUTPUTS
NO E_STOPINPUTS
OU
TPU
T 1
+24
VDC
OU
TPU
T 2
+12
VDC
24VDC
12VDC
201 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
A+OUT 1 2
15AATDR15
FU410
Vin-
Vin+
PS408
18V -32VDC /24VDC,12A ;12VDC,2A
POWER SUPPLY
VI-QCW31-ESYVICOR
VI-QCW31-ESY
GND
2 GBUS_BAR
5 3CR504E-STOP
/5/501
4081 4082
18AWGBLU4082
14AWGBLU4083
14AWGBLU4091
14AWGWHT/BLU4111
TB1PE
10414AWGGRN/YEL
4130
Disable+
Disable-
BSENSE+
CTRIM
DSENSE-
EOUT-
A+OUT
BSENSE+
CTRIM
DSENSE-
EOUT-
1 2
2A
FERRAZ SCHWAMUTATDR2
FU424
1 2
3 4
20A
FERRAZ SHAWMUT
ATDR20
FU409
18AWGBLU/WHT4371
14AWGWHT/BLU4201
18AWGBLU4242
18AWGBLU4241
1TB1PE
103
1TB1PE
105
14AWGWHT/BLU4222
18AWGBLU/WHT4372
PS23/323
+24V_1 / 5/502
PS13/323
+24V_2 / 11/1102
0V_1 / 5/502
12V_1 / 9/919
0V_2 / 9/921
501
502
503
504
505
506
507
508
509
510
511
512
513
514
515
516
517
518
519
520
521
522
523
524
525
526
527
528
529
530
531
532
533
534
535
536
537
538
539
540
JASON LEMOS Next page:Page Group:Previous page:
1746
Page:5
HWSS CIRCUIT
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
HOUR METER
2
(HARDWARE SYSTEM SAFETY)
01 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
11 14
CR513RESET
/5/514
11 12
CR509E_HWSS
/5/510
2
c no1NO, 24VDC
IDECHW1L-M1F10QD-S-24
/11/1133
PB514RESET
TB125
TB11 11 12
PB504E-STOP
2NC
IDECHW1E-LV4F02QD-R-24V
/8/816/5/521
8 7
15A,24VDC,SPDP
OMRONLY1N-D2-DC24V
CR504
EMERGENCY/ HWSS
5 3 /4/408
x1 x2
RED/5/504/8/816
PB504
EMERGENCY/ HWSS (LAMP)
A1 A2
24V,6A,2 PDT
PHOENIX CONTACTPLC-RSC-24DC/21-21
CR513
RESET
11 14 /5/504
21 24 /8/830
5141
5211
504650435042 5044
A1 A2
24V,6A,2 PDT
PHOENIX CONTACTPLC-RSC-24DC/21-21
CR509
11 12 /5/521
11 14 /5/517
21 24 /5/507
HM529
701DR001O1248D2CURTIS INSTRUMENT
1 2
4082
4082 26
TB1
40
TB141
TB13
321 24
CR1225
/12/1225
5261
11 14
CR1231SOFT ENABLE
/12/1231
ncc
TSH2002OVERTEMPERATURE
90 C +/- 5 C, NC
CANTHERMRA20AB117B250CO179
ncc
PSH2100OVERPRESSURE
GEM SENSORSPS61-19-2MNS-B-TS
A1 A2
24V,6A,2 PDT
PHOENIX CONTACTPLC-RSC--24DC/21-21
CR531
OVERTEMPERATURE
11 14 /5/504
21 24 /8/808
A1 A2
24V,6A,2 PDT
PHOENIX CONTACTPLC-RSC-24DC/21-21
CR535
OVERPRESURE
11 14 /5/504
21 24 /7/709
11 14
CR531OVERTEMPERATURE
/5/531
11 14
CR535OVERPRESURE
/5/536
5045
22AWGRED5311
22AWGBLK5314
20AWGBLU5314
18AWGRED5361
18AWGBLK5364
20AWGBLU5364
20AWGBLU5041
20AWGBLU5041
20AWGBLU/WHT4201
20AWGBLU/WHT4201
18AWGBLU5041
11 14CR1225
STACK ENABLE (PLC)
/12/1225
11 14CR509HWSS-OK
/5/510
P5311
P531
2
A1 A2
500A,24V
TYCO ELECTRONICSEV200AAANA
CR519STACK ENABLE
1 2 /3/317
A1 A2
500A,24VDC
TYCO ELECTRONICEV200AAANA
CR517STACK ENABLE
1 2 /3/317
x1x2V517400V;1A
GENERAL SEMICONDUCTOR1N 4004
x1x2V519400V;1A
GENERAL SEMICONDUCTOR1N 4004
P5171
P5191
2
2
5171 5172
20AWGBLU5170
20AWGBLU5170
TB194
95
96
97
20AWGBLU/WHT4201
20AWGBLU/WHT4201
3x22AWG/5/531
W5313x22AWG
/5/531W531
3x22AWG/5/535
W5363x22AWG
/5/535W536
20AWGRED5312
20AWGBLK5313
18AWGRED5362
18AWGBLK5363
21 24
CR509
/5/510
1 2
3 4
56
20AWGBLU8272
P536A
P536B
+24V_14/405
+24V_16/602
0V_14/420
0V_16/602
0V_Relay9/916
24V_PB8/815
0V_PB11/1130
24V_relay7/707
DI / 8/827
601
602
603
604
605
606
607
608
609
610
611
612
613
614
615
616
617
618
619
620
621
622
623
624
625
626
627
628
629
630
631
632
633
634
635
636
637
638
639
640
JASON LEMOS Next page:Page Group:Previous page:
1757
Page:6
CONTROL SYSTEM
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
DB 9 CONNECTOR
DB 9 CONNECTOR
POWER/DATA CONNECTOR
CAN INTERFACE
CPC:796190-1TYCO
P614P614
X1 X1
ON
1 2 3 4
RUN(1:ON;2-3OFF; 5-7:OFF;8: OFF)
PROGRAMMING(8:ON)
5 6 7 8OFF
DIP switch 8 segments
201 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
4:ON :CI TEMPERATURE
U625LCD DISPLAY
MATRIX ORBITAL
LK204-25-WB-VPT
CS604/7/703/8/803/9/903
/10/1004/11/1103/12/1201/13/1304
24INPUTS;18OUTPUTS
CONTROL SYSTEM
IFMCR0301
X1:01 Ub
X1:03 CAN _L
X1:04 CAN_H
X1:05 CAN_L
X1:06 CAN_H
X1:02GND
RS 232:02 RxD
RS 232:03 TxDRS 232:05GND
RS 232:06 UbRS 232:09 TEST
2 TxD
3 RxD
P/D:4GND
9 PWR
P/D:1 PWR
5 GND
P/D:3 Tx
P/D:2 Rx
TB14
TB1274082
20AWGBLU6071
20AWGBLU/WHT6072
24AWGRED6131
24AWGORG6141
20AWGBLK6281
4201
20AWGRED6291
20AWGGRN6081
20AWGYEL6091
x1
x2
R2120ohm
TB199
101
PDC1/6/627
PDC1/6/626
24AWGGRN6281
24AWGRED6131
24AWGORG6141
RS232/6/615
W626
RS232/6/627
W626
/6/627W628
/6/628W628
P61313
14
+24V_15/538
0V_15/533
+24V_17/701 0V_1
7/702
CAN_H /
CAN_L /
701
702
703
704
705
706
707
708
709
710
711
712
713
714
715
716
717
718
719
720
721
722
723
724
725
726
727
728
729
730
731
732
733
734
735
736
737
738
739
740
JASON LEMOS Next page:Page Group:Previous page:
1768
Page:7
DIGITAL INPUTS
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
%IX1.0
%IX1.8
%IX2.0
%IX2.8
%IX3.0
%IX3.8
%IX4.0
%IX4.8
OVERPRESSURE
INLET TANK LOW LEVEL
INLET TANK HIGH LEVEL
H2 GAS DETECTOR
C NO
C NC
01 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS 2
CS604
/8/803/9/903
/10/1004/11/1103/12/1201/13/1304
/6/605
Ub9
IN0001
IN0102
IN0203
IN0304
IN0506
IN0607
IN0708
LSH4003
INLET TANK HIGH LEVEL
MODE D-ON(HIGH LEVEL)
SUNXEX-F1
IN0405
2GND
1
Vcc
GD10005-40V DC; OUT:0-3V
HK-GH-A080C-W50A-05-R1-S1-E2-I2NEODYM TECHNOLOGIES INC.
29
P7341
5
RLY2
2
P7343
P7381
6
2
P7241
P7202
4
RLY1
3
Vout/Iout
X4/8/804
P7383
P7201
P7272
P7271
P7242
TB128
TB15
42014082
BLU7362
BLU7392
BRN7382
BRN7352
22AWGWHT7314
FSL1007
PUMP DI WATER FLOW SWITCH
GEMS SENSOR177592
22AWGWHT7274
20AWGRED7273
22AWGWHT7244
20AWGRED7243
22AWGWHT7204
20AWGRED7203
20AWGBLU7161
BLK7383
20AWGBLU7131
BLK7353
22AWGRED7311
20AWGRED7272
22AWGRED7271
20AWGRED7242
22AWGRED7241
20AWGRED7202
22AWGRED7201
22AWGRED7351
22AWGBLK7361
22AWGRED7381
22AWGBLK7391
20AWGBLK7051
20AWGRED7041
PS2026
PRESSURE DEMAND SWITCH
ASCO VALVE CANADAPA10A/RG10A21
20AWGWHT7064
7
8
TB150
52
53
54
55
56
57
20AWGBLU7064
20AWGBLU7131
20AWGBLU7161
20AWGBLU7314
20AWGBLU7274
20AWGBLU7244
20AWGBLU7204
GND10
21 24
CR535
/5/536
TB151
20AWGBLU5170
20AWGBLU7081
A2 A1
CR735
24V,6A,1 PDT
PHOENIX CONTACTPLC-RSC-24DC/21
11 14 /7/713
A2 A1
CR738
24V,6A,1 PDT
PHOENIX CONTACTPLC-RSC-24DC/21
11 14 /7/716
11 14
CR735
/7/735
11 14
CR738
/7/738
20AWGBLU/WHT7354
20AWGBLU/WHT7384
TB148
TB149
22AWGWHT7354
22AWGWHT7384
20AWGBLU7081
20AWGBLU5170
20AWGBLU5170
20AWGBLU5170
3x22AWG/7/720
W720
3x22AWG/7/719
W720
3x22AWG/7/723
W7243x22AWG
/7/723W724
3x22AWG/7/726
W7273x22AWG
/7/727W727
3x22AWG/7/730
W7303x22AWG
/7/730W730
3x22AWG/7/734
W7343x22AWG
/7/734W734
3x22AWG/7/738
W7383x22AWG
/7/738W738
NOC
GEM SENSORS164870
LSL1000DI TANK LOW LEVEL
NOC
GEM SENSORS164870
LSH1000
DI TANK HIGH LEVEL
3x22AWG/7/705
W703
3x22AWG/7/703
W703
LSL4003
INLET TANK LOW LEVEL
MODE D -ON (LOW LEVEL)
SUNXEX-F1
+24V_18/802
+24V_16/638
0V_16/638
0V_113/1303
24V_relay5/529
24V_relay7/733
24V_relay7/718
24V_relay8/806
801
802
803
804
805
806
807
808
809
810
811
812
813
814
815
816
817
818
819
820
821
822
823
824
825
826
827
828
829
830
831
832
833
834
835
836
837
838
839
840
JASON LEMOS Next page:Page Group:Previous page:
1779
Page:8
DIGITAL INPUTS
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
SYSTEM READYHWSS OK
SPARE
E-STOP
RESET
CUSTOMER INTERFACE
%IX5.0
%IX5.8
%IX6.0
%IX6.8
%IX7.0
%IX7.8
%IX8.0
%IX8.8
OVERTEMPERATURE
START
STOP
OPTIONALREMOVE JUMPER WHEN CONNECT
JMP
01 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS 2
22 21
PB504E-STOP
/5/504/5/521
IN0811
IN0912
CS604
/7/703/9/903
/10/1004/11/1103/12/1201/13/1304
/6/605
IN1013
IN1114
IN1215c no
1NO
IDECHW1L-M1F10-QD-G-24
/11/1137
PB820START
IN1316
IN1417
IN1518
X4/7/705
c nc
1NC
IDECHW1B-M1F01-R
PB822STOP
20AWGBLU8272
20AWGBLU8231
20AWGBLU8201
20AWGBLU8161
20AWGBLU5041
20AWGBLU5041
EXTERNAL DETECTOR
EXTERNAL DETECTOR
TB158
59
93
61
62
63
64
TB19 1 2
2A
FU812
20AWGBLU8121
20AWGBLU8122
20AWGBLU8123
21 24
CR513RESET
/5/514
21 24
CR531
/5/531
6520AWGBLU
8301
TB192
20AWGBLU8081
20AWGBLU5170
20AWGBLU5170
20AWGBLU8021
20AWGBLU8272
20AWGBLU8231
20AWGBLU8201
20AWGBLU8161
20AWGBLU8123
20AWGBLU8301
20AWGBLU8081
+24V_112/1218
+24V_17/739
24V_relay7/739
24V_PB5/526
DI /5/502
901
902
903
904
905
906
907
908
909
910
911
912
913
914
915
916
917
918
919
920
921
922
923
924
925
926
927
928
929
930
931
932
933
934
935
936
937
938
939
940
JASON LEMOS Next page:Page Group:Previous page:
17810
Page:9
ANALOGUE INPUTS
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
4-20mA
4-20mA
0.5-4.5V
0-5V
SW2:
SW3: ON
1 2 3 4 OpenClose
1 2CloseOpen3 4
0-5 S
201 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
J/2123
54V36V24V
SENSOR CONNECTIONS
Signal IN (RED)Signal RETURN (BLACK)Temperature IN (WHITE )
A_IN0001
RIT1100/9/903
CELL CONSTANT=0.01/CM
SENSOR
3-2839-3+GF+SIGNET
1
3V-
A_IN0102
1 V+
CS604
/7/703/8/803
/10/1004/11/1103/12/1201/13/1304
/6/605
A_IN0203
A_IN0304
4 SHIELD
3 TEMP IN
2 ISO GND
VM1500
STACK VOLTAGE MONITORING
MCR-VDC-UI-B-DC
PHOENIX CONTACT
1 SIGNAL IN
2
3
4
RIT1100/9/902
12-24VDC,4-20mA
CONDUCTIVITY MONITORING
3-2850-62+GF+ SIGNET
2
CM1500
+300A/OUT:0.5-4.5VDC
CURRENT MONITORING
DCS36-300-1InPOWER
BOUTPUT
A +12VDC
C SIG. GND
D POWER GND
X2/10/1005
13+24VDC
15GND3
7 +28V
8 GND1
9OUT I
11GND2
22AWGWHT9291
18AWGBLK9241
18AWGBLU3262
18AWGBLU3282
20AWGBLU9151
22AWGRED9081
20AWGRED9031
20AWGBLK9041
20AWGWHT9051
TB112
TB166
67
68
69
AFS1000
AIR FLOW SENSOR
D6F-W04A1OMRON
2OUTPUT
1 +12VDC
3 SIG. GND
TB146
22AWGBRN9272
22AWGBLK9301
P9271
2
P927
3
4318AWGRED
9211
22AWGRED9271
22AWGBLU9302 20AWGBLU
9291
Ub5
GND6
20AWGBLU/WHT4201
4618AWGWHT
9231
22AWGBLK9291
18AWGBLU/WHT4371
20AWGBLU12201
22AWGWHT9084
20AWGBLU9152
20AWGBLU9152
20AWGBLU9084
18AWGGRN9221
20AWGBLU9221
3x22AWG/9/928
W927
3x22AWG/9/926
W927
3x22AWG/9/908
W9083x22AWG
/9/908W908
TB142
18AWGBLU4242
TB145
TB113
12V_14/424
0V_24/435
0V_210/1020
DC+ / 3/326
DC- / 3/328
0V_Relay5/538
0V_Relay12/1223
12V_110/1019
An_INPUT_CURR112/1219
An_INPUT_CURR10/1003
1001
1002
1003
1004
1005
1006
1007
1008
1009
1010
1011
1012
1013
1014
1015
1016
1017
1018
1019
1020
1021
1022
1023
1024
1025
1026
1027
1028
1029
1030
1031
1032
1033
1034
1035
1036
1037
1038
1039
1040
JASON LEMOS Next page:Page Group:Previous page:
17911
Page:10
ANALOGUE INPUTS
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
4-20mA
4-20mA
0-10V
0-10V
201 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
P1013
A
P1013
B
P1022
1
P1022
3
P1006
1
X2/9/906
A_IN0407
A_IN0508
CS604
/7/703/8/803/9/903
/11/1103/12/1201/13/1304
/6/605
A_IN0609
TE2010
TEMPERATURE TRANSMITTER O2 REACTOR
ASSEMBLY SENS TEMP
2
21
x2x1
R1033
2K
TE1004
TEMPERATURE TRANSMITTER O2 STACK
ASSEMBLY SENS TEMP
x2x1
R1024
2K
3
PT10100-200PSI
PRESSURE TRANSMITTER O2 STACK
100.200.1.1.2.7NOSHOK
a + b-
c not used
b-
1
a +
A_IN0710
3
c not used
PT11000-200PSI
PRESSURE TRANSMITTER H2 STACK
100.200.1.1.2.7NOSHOK
P1031
3
P1031
1
P1031
2
P1022
2
P1006
2
10222 10223
10262
10312
10352
10313
22AWGBLK10351
22WGRED10311
22AWGRED10221
22AWGBLK10261
20AWGWHT10133
20AWGRED10132
22AWGRED10131
22AWGWHT10054
20AWGWHT10053
20AWGRED10052
22AWGRED10051
TB111
TB147
TB144
TB170
TB171
72
73
20AWGBLU12201
20AWGBLU10054
20AWGBLU10134
20AWGBLU10224
20AWGBLU10314
22AWGWHT10134
22AWGWHT10224
22AWGWHT10314
3x22AWG/10/1006
W10063x22AWG
/10/1006W1006
3x22AWG/10/1012
W10133x22AWG
/10/1012W1013
3x22AWG/10/1021
W10223x22AWG
/10/1021W1022
3x22AWG/10/1030
W10313x22AWG
/10/1030W1031
x1 x2
THERMISTOR
x1 x2
THERMISTOR
3
C
0V_29/934 12V_1
9/923
An_INPUT_CURR9/916
1101
1102
1103
1104
1105
1106
1107
1108
1109
1110
1111
1112
1113
1114
1115
1116
1117
1118
1119
1120
1121
1122
1123
1124
1125
1126
1127
1128
1129
1130
1131
1132
1133
1134
1135
1136
1137
1138
1139
1140
JASON LEMOS Next page:Page Group:Previous page:
171012
Page:11
DIGITAL OUTPUTS
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
%QX0.0
%QX0.8
%QX1.0
%QX1.8
%QX2.0
%QX2.8
%QX3.0
%QX3.8
PWM
PWM
201 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
P1120
1
P1116
2
P1120
2
OUT0203
OUT0102
OUT0001
CS604
/7/703/8/803/9/903
/10/1004/12/1201/13/1304
/6/605
OUT0304
X3
Ucom0210
OUT0406
OUT0507
OUT0608
OUT0709
Ucom0105
X2x1
X3
SV4003DI FEED WATER IN
ASCO VALVE CANADAEF8223G10-24VDC
X2X1
X3
SV3005O2 VENT VALVE
ASCO VALVE CANADA8262G134-24VDC
X2X1
X3
SV2019H2 SUPPLY VALVE
ASCO VALVE CANADA8327G42-24VDC
P1116
1
TB120
21
TB135
4123
4123
14 AWG WHT/BLU4221
18AWGRED11151
18AWGRED11152
18AWGRED11153
18AWGBLK11154
18AWGRED11201
18AWGRED11202
18AWGRED11203
18AWGBLK11204
18AWGRED11251
18AWGBLK11254
18AWGRED11071
18AWGBLU11070
18AWGBLU11241
1 2
FAV100024V DC,250CFM
VENTILATION FAN PROCESS ENCLOSURE
DV6224EBMPAPST
M
P1130
1
P1130
218AWGBLK
1127218AWGBLK
1127318AWGBLK
11274
TB137
TB136
TB175
TB176
77
TB178
20AWGBLU11271
20AWGBLU11251
20AWGBLU11201
20AWGBLU11151
18AWGRED11271
x1 x2
GREEN/8/820
PB820
START&RUN4201
20AWGBLU11321
20AWGBLU11371
80
81
x1 x2
BLU/5/514
PB514
FAULT
P1107
A 21
FAHX 1004
FAN COOLING WATER 734SLC3A01
THERMATRON
M P1107
B18AWGBLK
1107318AWGRED
11072
TB134
TB174
79
20AWGBLU11071
20AWGBLU11111
18AWGBLK11074
20AWGBLU11321
20AWGBLU11371
3x18AWG/11/1106
W11073x18AWG
/11/1106W1107
3x18AWG/11/1115
W11163x18AWG
/11/1115W1116
3x18AWG/11/1119
W11203x18AWG
/11/1119W1120
3x18AWG/11/1123
W11243x18AWG
/11/1124W1124
3x18AWG/11/1128
W11303x18AWG
/11/1128W1130
C18AWGGRN
11075
318AWGGRN
11155
318AWGGRN
11205
18AWGGRN11255
18AWGGND11275
P1124
1
P1124
2
3
+24V_212/1201
+24V_24/408
0V_211/1139
0V_211/1103
0V_PB5/528
1201
1202
1203
1204
1205
1206
1207
1208
1209
1210
1211
1212
1213
1214
1215
1216
1217
1218
1219
1220
1221
1222
1223
1224
1225
1226
1227
1228
1229
1230
1231
1232
1233
1234
1235
1236
1237
1238
1239
1240
JASON LEMOS Next page:Page Group:Previous page:
171113
Page:12
DIGITAL OUTPUTS
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
R4
R3
R0
R2
R1
%QX4.0
%QX4.8
%QX5.0
%QX5.8
%QX6.0
201 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
P1207
A
P1213
1
P1207
B21
H2 COOLING FAN
731SLM3A02-01THERMATRON
M
P1213
2
CS604
/7/703/8/803/9/903
/10/1004/11/1103/13/1304
/6/605
OUT08_NC01
OUT10_NC09
n.c.12
n.c.04
X5.1
Ucom0302
n.c.08
Ucom0406
OUT09_NO07
OUT09_NC05
OUT08_NO03
OUT11_NC13
OUT12_NC17
Ucom0510
OUT10_NO11
TB19
OUT11_NO15
Ucom0614
21
PMP1003 24VDC
DI WATER CIRCULATION PUMPMY2-8000.0019
SPECK PUMPEN
M
OUT12_NO18
Ucom1216
TB114
TB110
TB122
23
4082
18AWGBLK12074
20AWGBLU/WHT12073
20AWGBLU12072
18AWGRED12071
18AWGBLK12134
18AWGBLK12133
18AWGRED12132
18AWGRED12131
20AWGBLU12311
20AWGBLU12251
20AWGBLU12191
18AWGBLU12121
20AWGBLU12061
TB138
39
TB182
84
1 2
5A
FERRAZ SCWAMUTATDR 5
FU1213
18AWGBLU12130
20AWGBLU12201
A1 A2
24V,6A,1 PDT
PHOENIX CONTACTPLC-RSC-24DC/21
CR1231
SYSTEM ENABLE (SOFT)
11 14 /5/504
A1 A2
CR1225
ENABLE POWER STACK24V,6A,2 PDT
PHOENIX CONTACTPLC-RSC-24DC/21-21
11 14 /5/517
21 24 /5/528
TB185
TB186
20AWGBLU12071
20AWGBLU12252
20AWGBLU12312
20AWGBLU/WHT4201
21
FAHX 2003/12/1204
M
TB183
4221
3x18AWG/12/1204
W12073x18AWG
/12/1204W1207
3x18AWG/12/1213
W12133x18AWG
/12/1213W1213
C18AWGBLK
12075
21731SLM3A02-01
THERMATRON
M21FAHX 2031
/12/1209
O2 COOLING FAN
M
3x18AWG/12/1209
W12103x18AWG
/12/1209W1210
18AWGBLK12104
20AWGBLU/WHT12103
20AWGBLU12102
18AWGRED12101
18AWGBLK12105
P1210
A
P1210
B
C
+24V_211/1138
+24V_213/1303
0V_2
0V_Relay9/918
+24V_18/839
An_INPUT_CURR1 / 9/905
1301
1302
1303
1304
1305
1306
1307
1308
1309
1310
1311
1312
1313
1314
1315
1316
1317
1318
1319
1320
1321
1322
1323
1324
1325
1326
1327
1328
1329
1330
1331
1332
1333
1334
1335
1336
1337
1338
1339
1340
JASON LEMOS Next page:Page Group:Previous page:
171214
Page:13
DIGITAL OUTPUTS
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
R9
R8
R7
R6
R5%QX6.8
%QX7.0
%QX7.8
%QX8.0
%QX8.8
201 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
1 2
PMP1000PUMP FEED WATER
8841-2M03-B594AQUATEC
M
CS604
/7/703/8/803/9/903
/10/1004/11/1103/12/1201
/6/605
OUT13_NC01
n.c.04
X5.2
OUT13_NO03
Ucom0802
x2x1
X3
SV2013
DRYER UP VALVE
ASCO VALVE CANADA8327G42-24VDC
x2x1
X3
SV2018DRYER REGEN B VALVE
ASCO VALVE CANADA 8262G134 - 24VDC
OUT14_NC05
OUT14_NO07
Ucom0906
n.c.08
x2x1
x3
SV2014
DRYER REGEN A VALVE
ASCO VALVE CANADA 8262G134 - 24VDC
n.c.12
OUT15_NC9
OUT15_NO11
Ucom1010
x2x1
X3
SV2012
DRYER IN VALVE
ASCO VALVE CANADA8327G42-24VDC
OUT16_NC13
OUT16_NO15
Ucom1114
1 2
MT130924VDC, 130 CFM VENTILATION FAN ELECTRICAL CABINET
4715KL-05W-B59-P00TEHNOLOGIES CORPORATION
M
OUT17_NC17
OUT17_NO18
Ucom1216
P1314
1
P1321
1
P1323
1
P1327
1
P1333
1
P13142
P1321
2
P1323
2
P1327
2
P1333
2
TB115
16
17
18
19
TB132
TB130
4083
20AWGBLU13081
18AWGBLK13141
18AWGRED13271
18AWGRED13331
20AWGBLU/WHT13082
18AWGRED13142
18AWGBLK13143
18AWGBLK13144
18AWGRED13202
18AWGRED13203
18AWGRED13232
18AWGRED13233
18AWGBLK13204
18AWGBLK13234
18AWGRED13272
18AWGRED13273
18AWGBLK13274
18AWGRED13332
18AWGRED13333
18AWGBLK13334
20AWGBLU13061
18AWGBLU13121
20AWGBLU13251
20AWGBLU13191
20AWGBLU13311
1 2
MT1305
VENTILATION FAN ELECTRICAL CABINET
M
33
TB187
TB188
TB189
90
91
1 2
2A
FU1314
20AWGBLU13201
20WGBLU13271
20AWGBLU13331
18AWGBLU13140
x2x1
x3
SV1127
FEED WATER VALVE
ASCO VALVE CANADA8262G86-24VDC
P1311
2
P1311
1
TB131
20AWGBLU13081
18AWGRED13122
18AWGBLK13123
18AWGBLK13124
18AWGRED13121
3x18AWG/13/1311
W13113x18AWG
/13/1311W1311
3x18AWG/13/1314
W13143x18AWG
/13/1314W1314
3x18AWG/13/1325
W1323
3x18AWG/13/1319
W13213x18AWG
/13/1319W1321
3x18AWG/13/1325
W1323
3x18AWG/13/1329
W13273x18AWG
/13/1329W1327
3x18AWG/13/1334
W13333x18AWG
/13/1334W1333
318AWGGRN
13125
3
3
318AWGGRN
13275
318AWGGRN
13335
18AWGGRN13235
18AWGBLK13205
+24V_212/1232
+24V_2
0V_17/739
0V_1
1401
1402
1403
1404
1405
1406
1407
1408
1409
1410
1411
1412
1413
1414
1415
1416
1417
1418
1419
1420
1421
1422
1423
1424
1425
1426
1427
1428
1429
1430
1431
1432
1433
1434
1435
1436
1437
1438
1439
1440
JASON LEMOS Next page:Page Group:Previous page:
171315
Page:14
SPARE
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
1501
1502
1503
1504
1505
1506
1507
1508
1509
1510
1511
1512
1513
1514
1515
1516
1517
1518
1519
1520
1521
1522
1523
1524
1525
1526
1527
1528
1529
1530
1531
1532
1533
1534
1535
1536
1537
1538
1539
1540
JASON LEMOS Next page:Page Group:Previous page:
171416
Page:15
GROUNDING
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
GROUND RAIL
2
CABLE SHIELDS:W927;W1006;W1013;W1022;W1031
GND CONNECTOR
EL PANEL GND SCREW
01 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
X1534
BACK PANEL COVER
FRAME RIGHT SIDE
AWG 4GRN/YEL
AWG 14GRN/YEL
FRAME LEFT SIDE
14AWGGRN/YEL
DOOR LEFT SIDE
DOOR RIGHT SIDE
14AWGGRN/YEL
14AWGGRN/YEL
14AWGGRN/YEL
14AWGGRN/YEL
GND
JASON LEMOS Next page:Page Group:Previous page:
171517
Page:16
PANEL LAYOUT
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
26 inch
28 in
ch
107TERMINALS
START RESET E-STOP DISCONNECTHOUR METER
LCD display
CURRENT SENSOR
STOPFAULT
inside panel
MT1
305
MT1
309
P1
P613
P517P519
ELECTRICAL PANEL
RIGHT SIDE: CABLES TO TERMINAL BLOCKS
ELECTRICAL PANEL-LAYOUT OF APPARRATUS
LEFT SIDE: CABLES TO TERMINAL BLOCKS
2
TB1
DUCT: G.5X2LG6COVER:C.5LG6
.5 inch DUCT: G.5X2LG6COVER:C.5LG6
.5 inch
DUCT: G.5X2LG6COVER:C.5LG6
.5 inch
6 in
ch6
inch
7 in
ch
7 in
ch
DUCT: F1.5X2LG6COVER:C1.5LG6
1.5 inch
DUCT: F2.0X2LG6COVER:C2.0LG6 2 inch
DUCT: G1X2LG6COVER:C1LG6
1 inch
1 inch
1 inch
2.5 inch
9.5
inch
3 in
ch
01 RELEASED 01/12/10 MS
1 inch
02 UPDATE 25/02/11 MS
CS604
CR0301
CR50
9PL
C -R
SC-2
4DC/
21-2
1
CR51
3PL
C -R
SC-2
4DC/
21-2
1
TB1
WEI.1020000000 (WDU2,5)WDU 2.5
19
TB1WDU 2.5
20
PB504HW1E-LV4F02QD-R-24V
PB820HW1L-M1F10-QD-G-24
HM529
701DR001O1248D2
VM15
00M
CR-V
DC-
UI-
B-D
C
U625
LK204-25-WB-VPT
CM1500
DCS36-300-1
PB822
HW1B-M1F01-R
FU12
13
USCC1I
FU13
14
USCC1I
CR53
1PL
C -R
SC-2
4DC/
21-2
1
CR53
5PL
C -R
SC-2
4DC/
21-2
1
CR12
25PL
C -R
SC-2
4DC/
21-2
1
CR73
5PL
C -R
SC-2
4DC/
21
CR73
8PL
C -R
SC-2
4DC/
21
DS307
OT63FT3S
FU41
0
USCC1I
FU42
4
USCC1I
FU81
2
USCC1I
FU40
9
USCC2I
CR519
EV200AAANA
PS408
VI-QCW31-ESY
CR517
EV200AAANA
FU320
FT FH
FU32
0CN
N 2
50
FU321
FT FH
FU32
1CN
N 2
50
FU32
6
USCC2I
ATD
R0.
5
ATD
R0.
510
0
ATD
R20
FUSE
,20A
, TIM
E D
ELAY
101
ATD
R20
ATD
R15
ATD
R2
ATD
R5
ATD
R2
ATD
R2
PB514HW1L-M1F10QD-S-24V
PB, WITH LAMP,BLUE,24V,1NO9
CR12
31PL
C -R
SC-2
4DC/
21REL
AY,2
9661
71,2
4V,6
A11
0
CR50
4LY
1N-D
2-D
C24V
REL
AY,2
4V,1
5A,S
PDP
111
JASON LEMOS Next page:Page Group:Previous page:
1716 Page:
17
CABLE CHART
of
Date NameRevision: Drawing number:HydrogenicsMississauga,Ontario,Canada,L5T 2N6
PEM ELECTROLYZER_rev2G
Project Manager: ELECTROLYZER
24/02/2011M.SUSTAC
Name Date
Approved By:
Created By:
Project number:220 ADMIRAL BLVD.
1038968Page Title:
Revision Number:
Customer: Description:
Checked By: M.XU
J.L.
CABLE SOURCE DESTINATION
W531
W536
W704
W720
W724
W727
W731
W734
W738
W908
W927
W1006
W1013
W1022
W1031
CABLE SOURCE DESTINATION
W1107
W1116
W1120
W1124
W1130
W1207
W1213
W1311
W1314
W1320
W1323
W1327
W1333
TSH2002 TB1(3;40)
PS2100 TB1(3;41)
GD703 TB1(5;28;50)
LSL1000
LSH1000
TB1(7;54)
TB1(7;55)
FSL1007
PS2026
TB1(8;56)
TB1(8;57)
LSL4003
LSH4003
TB1(6;29;48)
TB1(6;29;49)
RIT1100 TB1(12;66)
AFS1000 TB1(43;46;69)
PT1006
PT1010
TB1(11;70)
TB1(11;71)
TE1004
TE2010
TB1(44;47;72)
TB1(44;47;73)
FAHX1004 TB1(34;74)
SV3005 TB1(35;76)
SV2019
SV4003
TB1(35;77)
TB1(36;78)
FAV1000 TB1(37;79)
FAHX2003 TB1(38;82)
PMP1003 TB1(39;83)
SV1127 TB1(31;88)
PMP1000 TB1(31;88)
SV2012
SV2013
SV2014
SV2018
TB1(32;89)
TB1(32;89)
TB1(33;90)
TB1(33;91)
2
01 RELEASED 01/12/10 MS
02 UPDATE 25/02/11 MS
E- HYDROGENICS CORPORATION Revision 3
INSTALLATION, OPERATION AND MAINTENANCE MANUAL PEM ELECTROLYZER