Hydrogen safety#Cryogenics
{{Short description|Procedures for safe production, handling and use of hydrogen}}
Image:Hindenburg disaster.jpg is an example of a large hydrogen explosion.]]
Hydrogen safety covers the safe production, handling and use of hydrogen, particularly hydrogen gas fuel and liquid hydrogen. Hydrogen possesses the NFPA 704's highest rating of four on the flammability scale because it is flammable when mixed even in small amounts with ordinary air. Ignition can occur at a volumetric ratio of hydrogen to air as low as 4% due to the oxygen in the air and the simplicity and chemical properties of the reaction. However, hydrogen has no rating for innate hazard for reactivity or toxicity. The storage and use of hydrogen poses unique challenges due to its ease of leaking as a gaseous fuel, low-energy ignition, wide range of combustible fuel-air mixtures, buoyancy, and its ability to embrittle metals that must be accounted for to ensure safe operation.
Liquid hydrogen poses additional challenges due to its increased density and the extremely low temperatures needed to keep it in liquid form. Moreover, its demand and use in industry—as rocket fuel, alternative energy storage source, coolant for electric generators in power stations, a feedstock in industrial and chemical processes including production of ammonia and methanol, etc.—has continued to increase, which has led to the increased importance of considerations of safety protocols in producing, storing, transferring, and using hydrogen.{{cite web|url=https://www1.eere.energy.gov/hydrogenandfuelcells/pdfs/h2_safety_fsheet.pdf|publisher=Office of Energy Efficiency and Renewable Energy|title=Hydrogen Safety}}
Hydrogen has one of the widest explosive/ignition mix range with air of all the gases with few exceptions such as acetylene, silane, and ethylene oxide, and in terms of minimum necessary ignition energy and mixture ratios has extremely low requirements for an explosion to occur. This means that whatever the mix proportion between air and hydrogen, when ignited in an enclosed space a hydrogen leak will most likely lead to an explosion, not a mere flame.{{cite journal |last1=Utgikar |first1=Vivek P |last2=Thiesen |first2=Todd |year=2005 |title=Safety of compressed hydrogen fuel tanks: Leakage from stationary vehicles |journal=Technology in Society |volume=27 |issue=3 |pages=315–320 |doi=10.1016/j.techsoc.2005.04.005}}
There are many codes and standards regarding hydrogen safety in storage, transport, and use. These range from federal regulations,{{cite tech report|author=Cadwallader, L. C.|author2=Herring, J. S.|year=1999|title=Safety Issues with Hydrogen as a Vehicle Fuel|doi=10.2172/761801|url=https://www.osti.gov/servlets/purl/761801}} ANSI/AIAA,{{cite web |title=AIAA G-095-2004, Guide to Safety of Hydrogen and Hydrogen Systems |url=http://aero-defense.ihs.com/document/abstract/GFEIHBAAAAAAAAAA |access-date=2008-07-28 |publisher=AIAA |format=PDF}} NFPA,{{cite web |title=List of NFPA Codes & Standards |url=https://www.nfpa.org/Codes-and-Standards/All-Codes-and-Standards/List-of-Codes-and-Standards |publisher=NFPA}} and ISO{{Cite web |title=ISO/TC 197 – Hydrogen technologies |url=https://www.iso.org/committee/54560/x/catalogue/p/1/u/1/w/0/d/0 |website=www.iso.org}} standards. The Canadian Hydrogen Safety Program concluded that hydrogen fueling is as safe as, or safer than, compressed natural gas (CNG) fueling,{{cite web |title=Canadian Hydrogen Safety Program testing H2/CNG |url=http://www.hydrogenandfuelcellsafety.info/2007/jun/h2cng.asp |url-status=dead |archive-url=https://web.archive.org/web/20110721205150/http://www.hydrogenandfuelcellsafety.info/2007/jun/h2cng.asp |archive-date=2011-07-21 |access-date=2010-07-05 |work=Hydrogenandfuelcellsafety.info}}
Prevention
{{NFPA 704|Health = 0|Flammability = 4|Reactivity = 0|S= SA |caption=The fire diamond hazard sign for both elemental hydrogen gas and its isotope deuterium.{{Cite web |url=https://cameochemicals.noaa.gov/chemical/8729|title=Hydrogen |website=cameochemicals.noaa.gov|access-date=Nov 29, 2020}}{{Cite web |url=https://cameochemicals.noaa.gov/chemical/3073|title=Deuterium |website=cameochemicals.noaa.gov|access-date=Nov 29, 2020}}}}
There are a number of items to consider to help design systems and procedures to avoid accidents when dealing with hydrogen, as one of the primary dangers of hydrogen is that it is extremely flammable.{{cite journal |last1=Utgikar |first1=Vivek P. |last2=Thiesen |first2=Todd| title=Safety of compressed hydrogen fuel tanks: Leakage from stationary vehicles |journal=Technology in Society |year=2005| volume=27 |issue=3 |pages=315–320 |doi=10.1016/j.techsoc.2005.04.005}}
=Inerting and purging=
{{further|Inerting (gas)|Purging (gas)}}
Inerting chambers and purging gas lines are important standard safety procedures to take when transferring hydrogen. In order to properly inert or purge, the flammability limits must be taken into account, and hydrogen's are very different from other kinds of gases. At normal atmospheric pressure it is 4% to 75%, based on the volume percent of hydrogen in oxygen it is 4% to 94%, while the limits of the detonation potential of hydrogen in air are 18.3% to 59% by volume.{{cite web |last1=Kalyanaraman |first1=M |title='Only a question of time' until large hydrogen systems are stable |website=Riviera Maritime Media |language=en |date=4 September 2019 |url=https://www.rivieramm.com/videos/how-tonbsp-hydrogen-fuel-cell-uptake-56079}}{{cite web |author=Barbalace, Kenneth |title=Periodic Table of Elements - Hydrogen - H|url=http://environmentalchemistry.com/yogi/periodic/H.html#Physical}}{{cite web
| url= https://www.energy.gov/sites/prod/files/2014/03/f11/871916.pdf
| archive-url= https://web.archive.org/web/20060227001252/http://www.hq.nasa.gov/office/codeq/doctree/canceled/871916.pdf
| archive-date= February 27, 2006
| title= Safety Standard for Hydrogen and Hydrogen Systems
| last= Gregory | first= Frederick D.
|date= February 12, 1997 |publisher= NASA
| access-date= 2008-05-09 }} In fact, these flammability limits can often be more stringent than this, as the turbulence during a fire can cause a deflagration which can create detonation. For comparison the deflagration limit of gasoline in air is 1.4–7.6%, and of acetylene in air,[http://www.msha.gov/alerts/hazardsofacetylene.htm MSHA – Safety Hazard Information – Special Hazards of Acetylene] {{Webarchive|url=https://web.archive.org/web/20160122062046/http://www.msha.gov/alerts/hazardsofacetylene.htm |date=2016-01-22 }}. Msha.gov. Retrieved on 2012-07-13. 2.5–82%.
Therefore, when equipment is open to air before or after a transfer of hydrogen, there are unique conditions to take into consideration that might have otherwise been safe with transferring other kinds of gases. Incidents have occurred because inerting or purging was not sufficient, or because the introduction of air in the equipment was underestimated (e.g., when adding powders), resulting in an explosion.{{cite journal|author=Sarah Eck & Michael D. Snyder|title=Hydrogen Safety Fundamentals|journal=Chemical Engineering Progress |date=December 2021|pages=36–41}} For this reason, inerting or purging procedures and equipment are often unique to hydrogen, and often the fittings or marking on a hydrogen line should be completely different to ensure that this and other processes are properly followed, as many explosions have happened simply because a hydrogen line was accidentally plugged into a main line or because the hydrogen line was confused with another.{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory|title=Use of "Quick-Disconnect" Fittings Results in Laboratory Instrument Explosion|date=September 2017|url=https://h2tools.org/lessons/use-quick-disconnect-fittings-results-laboratory-instrument-explosion}}{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory|title=Hydrogen Tube Trailer Explosion|date=September 2017 |url=https://h2tools.org/lessons/hydrogen-tube-trailer-explosion}}{{cite web |website=H2Tools |publisher=Pacific Northwest National Laboratory|title=Hydrogen Lab Fire|date=September 2017 |url=https://h2tools.org/lessons/hydrogen-lab-fire}}
=Ignition source management=
{{see also|Minimum ignition energy|Electrical equipment in hazardous areas}}
The minimum ignition energy of hydrogen in air is one of the lowest among known substances at 0.02 mJ, and hydrogen-air mixtures can ignite with 1/10 the effort of igniting gasoline-air mixtures.{{cite book |last1=Lewis |first1= Bernard |last2= Guenther|first2=von Elbe |title=Combustion, Flames and Explosions of Gases |edition=2nd|year= 1961 |publisher= Academic Press, Inc.|location= New York|isbn= 978-0124467507 |page= 535}} Because of this, any possible ignition source has to be scrutinized. Any electrical device, bond, or ground should meet applicable hazardous area classification requirement.{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory|title=Fire at Hydrogen Fueling Station|date=September 2017 |url=https://h2tools.org/lessons/fire-hydrogen-fueling-station |quote=The initial source of fire was likely a release of hydrogen from a failed weld on a pressure switch.}}{{cite web|website=H2Tools |publisher=Pacific Northwest National Laboratory |title=Small Fire in Fule Cell Test Stand|date=September 2017|url=https://h2tools.org/lessons/small-fire-fuel-cell-test-stand|quote=An electrical short circuit occurred, causing a small electrical fire.}} Any potential sources (like some ventilation system designs{{cite web|website=H2Tools |publisher=Pacific Northwest National Laboratory|title=Incorrect Relief Valve Set Point Leads to Explosion|date=September 2017 |url=https://h2tools.org/lessons/incorrect-relief-valve-set-point-leads-explosion|quote=Contributing cause was poor design of the venting system, which was installed in a horizontal position, causing inadequate venting and buildup of static electricity.}}) for static electricity build-up should likewise be minimized, e.g. through antistatic devices.{{cite web |website=H2Tools|publisher=Pacific Northwest National Laboratory |title=Fuel Cell Evaporation Pad Fire |date=September 2017|url=https://h2tools.org/lessons/fuel-cell-evaporator-pad-fire|quote=One theory presented the possibility of a spark (caused by static electricity) being the source of the ignition that caused the fire. Due to the proximity of the fuel cell unit to a shrink-wrap packaging machine at the time of the incident, this seemed to be a plausible hypothesis.}}
Hot-work procedures must be robust, comprehensive, and well-enforced; and they should purge and ventilate high-areas and sample the atmosphere before work. Ceiling-mounted equipment should likewise meet hazardous area requirements (NFPA 497). Finally, rupture discs should not be used as this has been a common ignition source for multiple explosions and fires. Instead other pressure relief systems such as a relief valve should be used.{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory|title=Hydrogen Explosion Due to Inadequate Maintenance|date=September 2017 |url=https://h2tools.org/lessons/hydrogen-explosion-due-inadequate-maintenance|quote=As a corrective action, eliminate burst discs from hydrogen storage assembly. Redesign venting system for the pressure relief valves to prevent or inhibit moisture build up and allow moisture drainage.}}{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory|title=Hydrogen Explosion at Coal-Fired Power Plant|date=September 2017 |url=https://h2tools.org/lessons/hydrogen-explosion-coal-fired-power-plant|quote=Explore elimination of rupture disk PRDs and substitution of spring-style relief valves.}}
= Mechanical integrity and reactive chemistry =
{{see also|hydrogen embrittlement|high temperature hydrogen attack|passive autocatalytic recombiner}}
There are four main chemical properties to account for when dealing with hydrogen that can come into contact with other materials even in normal atmospheric pressures and temperatures:
- The chemistry of hydrogen is very different from traditional chemicals. E.g., with oxidation in ambient environments. And neglecting this unique chemistry has caused issues at some chemical plants.{{Cite web|url=https://www.chicagotribune.com/suburbs/lake-county-news-sun/ct-lns-waukegan-blast-safety-update-st-1219-20191218-2hp6o6hyxrc6df6b6lr6xwdjge-story.html|title=Waukegan plant explosion that killed four workers was preventable, federal officials say|last=Abderholden|first=Frank S.|website=chicagotribune.com|date=18 December 2019 |access-date=2020-01-06|quote=Engineering Systems, Inc. conducted an independent investigation into the root cause of the explosion, which determined the cause to be human error that resulted in the mistaken addition of an erroneous ingredient.}} Another aspect to be considered as well is the fact that hydrogen can be generated as a byproduct of a different reaction may have been overlooked, e.g. Zirconium and steam creating a source of hydrogen.[http://www.latimes.com/news/science/la-sci-japan-quake-reactor-qa-20110314,0,5470584.story Japanese engineers work to contain nuclear reactor damage], Los Angeles Times, March 14, 2011[http://www.world-nuclear.org/info/Safety-and-Security/Safety-of-Plants/Appendices/Chernobyl-Accident---Appendix-1--Sequence-of-Events/ Chernobyl Accident Appendix 1: Sequence of Events] {{Webarchive|url=https://web.archive.org/web/20160114215108/http://www.world-nuclear.org/info/Safety-and-Security/Safety-of-Plants/Appendices/Chernobyl-Accident---Appendix-1--Sequence-of-Events/ |date=2016-01-14 }}, World Nuclear Association, November 2009 This danger can be circumvented somewhat via the use of passive autocatalytic recombiners.
- Another major issue to consider is the chemical compatibility of hydrogen with other common building materials like steel.{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory |title=Automated Hydrogen Ball Valve Fails to Open Due to Valve Stem Failure|date=September 2017 |url=https://h2tools.org/lessons/automated-hydrogen-ball-valve-fails-open-due-valve-stem-failure |quote=valve stem material incompatibility with hydrogen (causing a material weakening) is suspected}}{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory|title=Gaseous Hydrogen Leak and Explosion|date=September 2017 |url=https://h2tools.org/lessons/gaseous-hydrogen-leak-and-explosion|quote=A GH2 leak occurred in an underground ASTM A106 Grade B, Schedule XX carbon steel pipe with a 3.5-inch diameter and a 0.6-inch wall thickness. The pipe was coated with coal tar primer and coal tar enamel, wrapped with asbestos felt impregnated with coal tar, coated with a second coat of coal tar enamel, and wrapped in Kraft paper, in accordance with American Water Works Association Standard G203. The source of the leak was an oval hole about 0.15 in x 0.20 in at the inner surface of the pipe and about 2-in in diameter at the outer surface of the pipe. Upon excavation of the pipe, it was noted that the coating was not present at the leak point. This resulted in galvanic corrosion over a 15-year period and the eventual rupture when high-pressure gas was applied to the thin pipe membrane. The pipe was 8 ft 9 in below the concrete pad.}} Because of hydrogen embrittlement, material compatibility with hydrogen is specially considered.
- These considerations can further change because of special reactions at high temperatures.
- The diffusivity of hydrogen is very different from ordinary gases, and therefore gasketing materials have to be chosen carefully.{{cite web|url=https://www.fmglobal.com/research-and-resources/fm-global-data-sheets |publisher=Factory Mutual|title=FM Global Hydrogen Datasheets (online): Hydrogen, Data Sheet ID# 7-91|date=April 2021}}{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory|title=Leak on Compressor at Fueling Station|date=September 2017|url=https://h2tools.org/lessons/leak-compressor-fueling-station|quote=This allowed greater movement of the shaft, which led to a shaft seal leaking hydrogen.}}
- The buoyant forces and stresses on mechanical bodies involved are often reversed from standard gases. For example, because of buoyancy, stresses are often pronounced near the top of a large storage tank.{{cite journal|url=http://www.eihp.org/public/documents/EIHP2_MTA_Proceedings_Volume_1_DVW.pdf|title=EIHP2 META Proceedings DVW|author=Schmidtchen, Ulrich|publisher=German Hydrogen Association|location=Brussels|date=2002-10-02|journal=EIHP}}
All four of these factors are considered during the initial design of a system using hydrogen, and is typically accomplished by limiting the contact between susceptible metals and hydrogen, either by spacing, electroplating, surface cleaning, material choice, and quality assurance during manufacturing, welding, and installation. Otherwise, hydrogen damage can be managed and detected by specialty monitoring equipment.The Australian Institute for Non Destructive Testing (AINDT), [http://www.ndt.net/apcndt2001/papers/1154/1154.htm Detection and Quantification of Hydrogen Damage] {{Webarchive|url=https://web.archive.org/web/20141129031443/http://www.ndt.net/apcndt2001/papers/1154/1154.htm |date=2014-11-29 }}
=Leaks and flame detection systems=
{{see also|hydrogen piping|hydrogen leak testing|hydrogen odorant}}
Locations of hydrogen sources and piping have to be chosen with care. Since hydrogen is a lighter-than-air gas, it collects under roofs and overhangs (typically referred to as trapping sites), where it forms an explosion hazard. Many individuals are familiar with protecting plants from heavier-than-air vapors, but are unfamiliar with "looking up", and is therefore of particular note. It can also enter pipes and can follow them to their destinations. Because of this, hydrogen pipes should be well-labeled and located above other pipes to prevent this occurrence.
Even with proper design, hydrogen leaks can support combustion at very low flow rates, as low as 4 micrograms/s.M.S. Butler, C.W. Moran, Peter B. Sunderland, R.L. Axelbaum, Limits for Hydrogen Leaks that Can Support Stable Flames, International Journal of Hydrogen Energy 34 (2009) 5174–5182. To this end, detection is important. Hydrogen sensors or a katharometer allow for rapid detection of hydrogen leaks to ensure that the hydrogen can be vented and the source of the leak tracked down. Around certain pipes or locations special tapes can be added for hydrogen detection purposes. A traditional method is to add a hydrogen odorant with the gas as is common with natural gas. In fuel cell applications these odorants can contaminate the fuel cells, but researchers are investigating other methods that might be used for hydrogen detection: tracers, new odorant technology, advanced sensors, and others.
While hydrogen flames can be hard to see with the naked eye (it can have a so-called "invisible flame"), they show up readily on UV/IR flame detectors. More recently Multi IR detectors have been developed, which have even faster detection on hydrogen-flames.{{cite web|publisher=Fire & Gas Technologies, Inc.|title=IR3 Flame Detector - FlameSpec-IR3-H2|url=https://www.fg-detection.com/flamespec-ir3-h2}}{{cite web |url=https://www.spectrex.net/en-us/flame-gas-detectors/flame-detectors/40-40-series/40-40m-multi-ir-flame-detector|author=spectrex|title=40/40M Multi IR Flame Detector}} This is quite important in fighting hydrogen fires, as the preferred method of fighting a fire is stopping the source of the leak, as in certain cases (namely, cryogenic hydrogen) dousing the source directly with water may cause icing, which in turn may cause a secondary rupture.{{cite web |url=http://www.phmsa.dot.gov/staticfiles/PHMSA/DownloadableFiles/Files/erg2008_eng.pdf |title=Emergency Response Handbook |year=2008 |publisher=Piplines and Hazardous Materials Safety Administration - Department of Transportation |page=115 |quote=Do not direct water at source of leak or safety devices; icing may occur. |archive-url=https://web.archive.org/web/20090603214959/http://www.phmsa.dot.gov/staticfiles/PHMSA/DownloadableFiles/Files/erg2008_eng.pdf |archive-date=3 June 2009 |url-status=dead}}
=Ventilation and flaring=
{{see also|flaring}}
Aside from flammability concerns, in enclosed spaces, hydrogen can also act as an asphyxiant gas. Therefore, one should make sure to have proper ventilation to deal with both issues should they arise, as it is generally safe to simply vent hydrogen into the atmosphere. However, when placing and designing such ventilation systems, one must keep in mind that hydrogen will tend to accumulate towards the ceilings and peaks of structures, rather than the floor. Many dangers may be mitigated by the fact that hydrogen rapidly rises and often disperses before ignition.{{cite journal |title=Emergency and Continuous Exposure Guidance Levels for Selected Submarine Contaminants|volume=2 |year=2008|journal=National Academies of Sciences, Engineering, and Medicine|location=Washington, DC |publisher=The National Academies Press |url=https://www.nap.edu/read/12032/chapter/9#154}}
In certain emergency or maintenance situations, hydrogen can also be flared.{{Cite web|url=https://appel.nasa.gov/2011/02/02/explosive-lessons-in-hydrogen-safety/|title=Explosive Lessons in Hydrogen Safety | APPEL Knowledge Services|website=appel.nasa.gov|date=2 February 2011 }} For example, a safety feature in some hydrogen-powered vehicles is that they can flare the fuel if the tank is on fire, burning out completely with little damage to the vehicle, in contrast to the expected result in a gasoline-fueled vehicle.{{Cite web|title=Hydrogen Car Safety Test- Fuel Leak H2 vs. Petrol|url=https://vimeo.com/302628955|website=Vimeo|language=en|access-date=2020-05-07}}
=Inventory management and facility spacing=
Ideally, no fire or explosion will occur, but the facility should be designed so that if accidental ignition occurs, it will minimize additional damage. Minimum separation distances between hydrogen storage units should be considered, together with the pressure of said storage units (cf., NFPA 2 and 55). Explosion venting should be laid out so that other parts of the facility will not be harmed. In certain situations, this translates to a roof that can be safely blown away from the rest of the structure in an explosion.
=Cryogenics=
{{see also|BLEVE}}
Liquid hydrogen has a slightly different chemistry compared to other cryogenic chemicals, as trace accumulated air can easily contaminate liquid hydrogen and form an unstable mixture with detonative capabilities similar to TNT and other highly explosive materials. Because of this, liquid hydrogen requires complex storage technology such as the special thermally insulated containers and requires special handling common to all cryogenic substances. This is similar to, but more severe than liquid oxygen. Even with thermally insulated containers it is difficult to keep such a low temperature, and the hydrogen will gradually leak away. Typically it will evaporate at a rate of 1% per day.Peter Kushnir. [http://www.almc.army.mil/alog/issues/MayJun00/MS492.htm Hydrogen As an Alternative Fuel ] {{webarchive|url=https://web.archive.org/web/20080808053811/http://www.almc.army.mil/alog/issues/MayJun00/MS492.htm |date=2008-08-08 }}. PB 700-00-3. Vol. 32, Issue 3, May–June 2000. almc.army.mil.
The main danger with cryogenic hydrogen is what is known as BLEVE (boiling liquid expanding vapor explosion). Because hydrogen is gaseous in atmospheric conditions, the rapid phase change together with the detonation energy combine to create a more hazardous situation.{{cite web|website=H2Tools |publisher=Pacific Northwest National Laboratory|title=Liquid Hydrogen Tank Boiling Liquid Expanding Vapor Explosion (Bleve) Due to Water-Plugged Vent Stack|date=September 2017 |url=https://h2tools.org/lessons/liquid-hydrogen-tank-boiling-liquid-expanding-vapor-explosion-bleve-due-water-plugged-vent|quote=Place signs on all liquid hydrogen tanks indicating that no water is to be put on the vent stack.}} A secondary danger is the fact that many materials change from being to ductile to brittle at extremely cold temperatures, allowing new places for leaks to form.
=Human factors=
Along with traditional job safety training, checklists to help prevent commonly skipped steps (e.g., testing high points in the work area) are often implemented, along with instructions on the situational dangers that come inherent to working with hydrogen.{{cite web|website=H2Tools|publisher=Pacific Northwest National Laboratory|title=Liquid Hydrogen Delivery Truck Offloading Valve Failure |date=September 2017|url=https://h2tools.org/lessons/liquid-hydrogen-delivery-truck-offloading-valve-failure}}
Incidents
Hydrogen codes and standards
There exist many hydrogen codes and standards for hydrogen fuel cell vehicles, stationary fuel cell applications and portable fuel cell applications. Additional to the codes and standards for hydrogen technology products, there are codes and standards for hydrogen safety, for the safe handling of hydrogen{{cite web |website=HySafe |url=http://www.hysafe.org/download/1710/HYSAFE_D113_version_1.1.pdf |title=Initial Guidance for Using Hydrogen in Confined Spaces |access-date=2012-07-13}} and the storage of hydrogen. What follows is a list of some of the major codes and standards regulating hydrogen:
class=wikitable |
Name of standard
! Short title |
---|
29CFR1910.103
| Gaseous and cryogenic hydrogen handling and storage |
29CFR1910.119 |
40CFR68
| Chemical accident prevention provisions |
49CFR
| Regulations on shipping and handling hydrogen gas and cryogenic hydrogen{{cite tech report|author=Cadwallader, L. C. |author2=Herring, J. S. |year=1999|title=Safety Issues with Hydrogen as a Vehicle Fuel|doi=10.2172/761801 |url=https://www.osti.gov/servlets/purl/761801}} |
ISO 13984:1999
| Liquid hydrogen — Land vehicle fuelling system interface |
ISO/AWI 13984
| Liquid Hydrogen Land Vehicle Fueling Protocol |
ISO/AWI 13985
| Liquid hydrogen — Land vehicle fuel tanks |
ISO/CD 14687
| Hydrogen fuel quality — Product specification |
ISO/AWI TR 15916
| Basic considerations for the safety of hydrogen systems |
ISO 16110
| Hydrogen generators using fuel processing technologies |
ISO 16111
| Transportable gas storage devices — Hydrogen absorbed in reversible metal hydride |
ISO/AWI 17268
| Gaseous hydrogen land vehicle refuelling connection devices |
ISO 19880
| Gaseous hydrogen — Fuelling stations |
ISO/AWI 19881
| Gaseous hydrogen — Land vehicle fuel containers |
ISO 19882
| Gaseous hydrogen — Thermally activated pressure relief devices for compressed hydrogen vehicle fuel containers |
ISO/TS 19883
| Safety of pressure swing adsorption systems for hydrogen separation and purification |
ISO/WD 19884
| Gaseous hydrogen — Cylinders and tubes for stationary storage |
ISO/CD 19885
| Gaseous hydrogen — Fuelling protocols for hydrogen-fueled vehicles — Part 1: Design and development process for fueling protocols |
ISO/CD 19887
| Gaseous Hydrogen — Fuel system components for hydrogen fuelled vehicles |
ISO/AWI 22734
| Hydrogen generators using water electrolysis — Industrial, commercial, and residential applications |
ISO/AWI 24078
| Hydrogen in energy systems — Vocabulary |
ISO 26142:2010
| Hydrogen detection apparatus — Stationary applications{{cite web|url=https://www.iso.org/committee/54560/x/catalogue/p/1/u/1/w/0/d/0|title=Standards and/or projects under the direct responsibility of ISO/TC 197 Secretariat of the International Organization for Standardization}} |
NFPA 2
| Hydrogen technologies code |
NFPA 30A
| Rules for design of refueling stations |
NFPA 50A
| Standard for gaseous hydrogen systems at consumer sites |
NFPA 50B
| Standard for liquefied hydrogen systems at consumer sites |
NFPA 52
| Compressed Natural Gas Vehicular Fuel Systems Code |
NFPA 57
| Liquefied natural gas vehicular fuel systems standard{{cite web |url=https://www.nfpa.org/Codes-and-Standards/All-Codes-and-Standards/List-of-Codes-and-Standards |title=List of NFPA Codes & Standards|publisher=NFPA}} |
CGA C-6.4
|Methods for External Visual Inspection of Natural Gas Vehicle (NGV) and Hydrogen Gas Vehicle (HGV) Fuel Containers and Their Installations |
CGA G-5
|Hydrogen |
CGA G-5.3
|Commodity Specification for Hydrogen |
CGA G-5.4
|Standard for Hydrogen Piping Systems at User Locations |
CGA G-5.5
|Hydrogen Vent Systems |
CGA G-5.6
|Hydrogen Pipeline Systems |
CGA G-5.7
|Carbon Monoxide and Syngas Pipeline Systems |
CGA H-3
|Standard for Cryogenic Hydrogen Storage |
CGA H-4
|Terminology Associated with Hydrogen Fuel Technologies |
CGA H-5
|Standard for Bulk Hydrogen Supply Systems (an American National Standard) |
CGA H-7
|Standard Procedures for Hydrogen Supply Systems |
CGA H-10
|Combustion Safety for Steam Reformer Operation |
CGA H-11
|Safe Startup and Shutdown Practices for Steam Reformers |
CGA H-12
|Mechanical Integrity of Syngas Outlet Systems |
CGA H-13
|Hydrogen Pressure Swing Adsorber (PSA) Mechanical Integrity Requirements |
CGA H-14
|HYCO Plant Gas Leak Detection and Response Practices |
CGA H-15
|Safe Catalyst Handling in HYCO Plants |
CGA H-16
|Guideline on Remedial Actions for HYCO Plant Components Subject to High Temperature Hydrogen Attack |
CGA P-6
|Standard Density Data, Atmospheric Gases and Hydrogen |
CGA P-28
|OSHA Process Safety Management and EPA Risk Management Plan Guidance Document for Bulk Liquid Hydrogen Supply Systems |
CGA P-74
|Standard for Tube Trailer Supply Systems at Customer Sites |
CGA PS-31
|CGA Position Statement on Cleanliness for Proton Exchange Membranes Hydrogen Piping/Components |
CGA PS-33
|CGA Position Statement on Use of LPG or Propane Tank as Compressed Hydrogen Storage Buffers |
CGA PS-46
|CGA Position Statement on Roofs Over Hydrogen Storage Systems |
CGA PS-48
|CGA Position Statement on Clarification of Existing Hydrogen Setback Distances and Development of New Hydrogen Setback Distances in NFPA 55 |
CGA PS-69
|CGA Position Statement on Liquefied Hydrogen Supply System Separation Distances |
= Guidelines =
The current ANSI/AIAA standard for hydrogen safety guidelines is AIAA G-095-2004, Guide to Safety of Hydrogen and Hydrogen Systems.{{cite web
| url= http://aero-defense.ihs.com/document/abstract/GFEIHBAAAAAAAAAA
| title= AIAA G-095-2004, Guide to Safety of Hydrogen and Hydrogen Systems
| format= PDF
| publisher= AIAA
| access-date = 2008-07-28}} As NASA has been one of the world's largest users of hydrogen, this evolved from NASA's earlier guidelines, NSS 1740.16 (8719.16). These documents cover both the risks posed by hydrogen in its different forms and how to ameliorate them. NASA also references Safety Standard for Hydrogen and Hydrogen Systems {{cite book|publisher=Office of Safety and Mission Assurance, National Aeronautics and Space Administration|title=Safety Standard for Hydrogen and Hydrogen Systems: Guidelines for Hydrogen System Design, Materials Selection, Operations, Storage, and Transportation |location=Washington, DC|date=1997-10-29|id=NASA TM-112540, NSS 1740.16}} and the Sourcebook for Hydrogen Applications.{{cite book|publisher=Hydrogen Research Institute and the National Renewable Energy Laboratory|title=Sourcebook for Hydrogen Applications|location=Quebec, CA|year=1998}}
Another organization responsible for hydrogen safety guidelines is the [https://www.cganet.com/ Compressed Gas Association (CGA)], which has a number of references of their own covering general hydrogen storage,{{cite book |publisher=Compressed Gas Association, Inc.|title=Hydrogen|edition=4th|location=Arlington, VA|year=1991}} piping,{{cite book |publisher=Compressed Gas Association, Inc.|title=Standard for Hydrogen Piping Systems|edition=1st |location=Arlington, VA|year=1992}} and venting.{{cite book |publisher=Compressed Gas Association, Inc.|title=Hydrogen Vent Systems|edition=1st|location=Arlington, VA|year=1996}}
In 2023 CGA launched the [https://safehydrogenproject.org/about/ Safe Hydrogen Project] which is a collaborative global effort to develop and distribute safety information for the production, storage, transport, and use of hydrogen.
See also
References
{{reflist}}
External links
- [http://www.hydrogenandfuelcellsafety.info Hydrogen and Fuel Cell Safety Report]
- [http://hysafe.org/IAHySafe The International Association for Hydrogen Safety]
- [http://www.explosionsolutions.org/MScHSE/ Higher Educational Programme in Hydrogen Safety Engineering]
- [http://www.explosionsolutions.org/kcehs/ Knowledge Center for Explosion and Hydrogen Safety]
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