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Hydrogen safety
Procedures for safe production, handling and use of hydrogen

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.

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.

There are many codes and standards regarding hydrogen safety in storage, transport, and use. These range from federal regulations, ANSI/AIAA, NFPA, and ISO standards. The Canadian Hydrogen Safety Program concluded that hydrogen fueling is as safe as, or safer than, compressed natural gas (CNG) fueling,

Prevention

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.9

Inerting and purging

Further information: Inerting (gas) and 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.1011121314 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,15 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.16 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.171819

Ignition source management

See also: Minimum ignition energy and 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.2021 Because of this, any possible ignition source has to be scrutinized. Any electrical device, bond, or ground should meet applicable hazardous area classification requirement.2223 Any potential sources (like some ventilation system designs24) for static electricity build-up should likewise be minimized, e.g. through antistatic devices.25

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).26 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.2728

Mechanical integrity and reactive chemistry

See also: hydrogen embrittlement, high temperature hydrogen attack, and 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.29 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.303132 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.3334 Because of hydrogen embrittlement, material compatibility with hydrogen is specially considered.35
  • These considerations can further change because of special reactions at high temperatures.36
  • The diffusivity of hydrogen is very different from ordinary gases, and therefore gasketing materials have to be chosen carefully.3738
  • 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.3940

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.4142

Leaks and flame detection systems

See also: hydrogen piping, hydrogen leak testing, and 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.43 Many individuals are familiar with protecting plants from heavier-than-air vapors, but are unfamiliar with "looking up", and is therefore of particular note.44 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.4546

Even with proper design, hydrogen leaks can support combustion at very low flow rates, as low as 4 micrograms/s.474849 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.50

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.5152 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.5354

Ventilation and flaring

See also: flaring

Aside from flammability concerns, in enclosed spaces, hydrogen can also act as an asphyxiant gas.55 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.5657

In certain emergency or maintenance situations, hydrogen can also be flared.5859 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.60

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.61

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.6263

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.64 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.65

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.6667

Incidents

DateLocationDescriptionSuspected cause
6 May 1937Naval Air Station LakehurstAs the zeppelin Hindenburg was approaching landing, a fire detonated one of the aft hydrogen cells, thereby rupturing neighboring cells and causing the airship to fall to the ground aft-first. The inferno then travelled towards the stern, bursting and igniting the remaining cells.Despite four news stations recording the disaster on film and surviving eyewitness testimonies from crew and people on the ground, the cause of the initial fire was never conclusively determined.
5 April 1975Ilford, UKAn oxygen separator exploded due to hydrogen ingress. The resulting abrupt release of lye exposed one person who later died of lye burn injuries.Mixing of oxygen and hydrogen due to breakdown of the electrolyser cells.68
28 January 1986Over the Atlantic Ocean just east of Kennedy Space CenterA large LH2 tank ruptured and exploded, killing all 7 astronauts aboard the Space Shuttle ChallengerA faulty O-ring on the solid rocket booster allowed hot gases and flames to impinge upon the external LH2 tank, causing the tank wall to weaken and then burst. The thrust generated from the contents of the tank caused the LOX tank above to also rupture, and this mixture of LH2/LOX then detonated, destroying the orbiter in the explosion.
1999Hanau, GermanyA large chemical tank used to store hydrogen for manufacturing processes exploded.The tank was designed to lie on its side, but instead was laid upright. The forces towards the top of the tank caused it to rupture and then explode.69
January 2007Muskingum River Coal Plant (owned and operated by AEP)An explosion of compressed hydrogen during delivery at the Muskingum River Coal Plant caused significant damage and killed one person.707172A premature rupture of a pressure relief disc used for the compressed hydrogen cooling system.73
2011Fukushima, JapanThree reactor buildings were damaged by hydrogen explosions.Exposed Zircaloy cladded fuel rods became very hot and reacted with steam, releasing hydrogen.7475 The containments were filled with inert nitrogen, which prevented hydrogen from burning in the containment. However, the hydrogen leaked from the containment into the reactor building, where it mixed with air and exploded.76 To prevent further explosions, vent holes were opened in the top of the remaining reactor buildings.
2015The Formosa Plastics Group refinery in TaiwanChemical plant explosionDue to hydrogen leaking from a pipe77
12 February 2018 13:20Diamond Bar, a suburb of Los Angeles, CAOn the way to an FCV hydrogen station, a truck carrying about 24 compressed hydrogen tanks caught fire. This caused the evacuation initially of a one-mile radius area of Diamond Bar. The fire broke out on the truck at about 1:20 p.m. at the intersection of South Brea Canyon Road and Golden Springs Drive, according to a Los Angeles County Fire Department dispatcher.78798081The National Transportation Safety Board has launched an investigation.82
August 2018Veridam El Cajon, CAA delivery truck carrying liquid hydrogen caught fire at Veridiam manufacturing plant.83 in El Cajon, California.84It is not known what caused the explosion.85
May 2019AB Specialty Silicones in Waukegan, IllinoisAn explosion killed four workers and seriously injured a fifth.Operator error adding an incorrect ingredient8687
23 May 2019Gangwon Technopark in Gangneung, South KoreaA hydrogen tank exploded, killing two and injuring six.8889Oxygen seeped into the hydrogen storage tanks.90
June 2019Air Products and Chemicals facility in Santa Clara, CaliforniaTanker truck explosion damaging surrounding hydrogen transfill facilityLeak in transfer hose.91 This resulted in the temporary shutdown of multiple hydrogen fueling stations in the San Francisco area.92
June 2019NorwayA Uno-X fueling station experienced an explosion,93 resulting in the shutdown of all Uno-X hydrogen fueling stations and a temporary halt in sales of fuel cell vehicles in the country.94Investigations determined that neither the electrolyzer nor the dispenser used by customers had anything to do with this incident.9596 Instead, Nel ASA announced the root cause of the incident had been identified as an assembly error of the use of a specific plug in a hydrogen tank in the high-pressure storage unit.97
December 2019An Airgas facility in Waukesha, WisconsinA gas explosion injured one worker and caused 2 hydrogen storage tanks to leak.9899Unknown.100
7 April 2020OneH2 Hydrogen Fuel plant in Long View, North CarolinaAn explosion caused significant damage to surrounding buildings. The blast was felt several miles away, damaging about 60 homes. No injuries from the explosion were reported.The incident remains under investigation.101102103104 The company published a press release: Hydrogen Safety Systems Operated Effectively, Prevented Injury at Plant Explosion.105
11 June 2020Praxair Inc., 703 6th St. Texas City, TexasAn explosion occurred at the hydrogen production plant.No further details106107
30 September 2020Changhua City, TaiwanA hydrogen tanker crashed and exploded, killing the driver.Vehicle crash108
9 August 2021Medupi Power Station in South AfricaAn explosion in Unit 4 of the plantImproper operator procedure while the generator was being purged of hydrogen109
25 February 2022Detroit, MichiganA hydrogen tank for a balloon in a pick-up truck bed exploded, injuring 2.The Detroit Fire Department believes a leak in the hydrogen tank caused the explosion.

110

22 April 2022Towanda, PennsylvaniaA hydrogen tank at Global Tungsten & Powders Corp. exploded. A spokesperson for the company said five employees were taken to hospitals with non-life-threatening injuries.OSHA and company officials are investigating the incident.

111112

28 September 2022Vasai, India3 people killed, 8 injured in hydrogen cylinder explosion in at a Maharashtra Industrial unit.Faulty tank.113114
6 February 2023Delaware County, OhioA pickup truck towing a trailer carrying full hydrogen tanks on US-23 in Delaware County Ohio explodes after crash. Three people were transported to a hospital with minor injuries.Vehicular crash115
28 April 2023Troutman, North CarolinaA Plug Power liquid hydrogen tanker venting and flaring caused an evacuation at a Pilot Travel Center in Troutman, North Carolina along the Charlotte Highway, Interstate 77.Safety flare and vent due to excess pressure.116117118119
18 July 2023Kern County, CaliforniaA Golden Empire Transit Bus was destroyed during fueling at their maintenance facility.Leaking fuel tank.120121122123
8 August 2023Lebring, Styria, AustriaAn outdoor hydrogen tank exploded at the premises of HypTec in Austria, causing massive damage due to the pressure wave which could be felt 3 km away. The personnel at the site was indoor and only minor injuries to an employee occurred.Leaky tank124125
17 September 2023North West Queensland, AustraliaRelease of pressurised hydrogen gas at a chemical plant in North West Queensland resulted in an explosion and fire. Three workers were injured and damage caused to plant. The incident occurred during the recommissioning of equipment after routine scheduled maintenance. The injured workers did not require hospitalisation.Failure of a butterfly valve, under hydrogen header-pressure of approximately 2000kPa. The bearing bush bolts of the butterfly valve may not have been correctly installed at the time of overhaul.126
26 June 2024Gersthofen, GermanyA fire broke out after an apparent explosion at a newly opened hydrogen filling station in the freight transport center in Gersthofen in Augsburg. No one was injured. The station remained closed after the incident.Probably an explosion in a compressor.127
19 September 2024Geismar, LouisianaA hydrogen gas explosion and fire occurred at Chevron Renewable Energy Group's renewable diesel plant. Two workers were seriously injured.Under investigation.128
23 December 2024Chungju, South KoreaA hydrogen gas explosion occurred in a bus after being refueled at a hydrogen filling station. Three persons were injured, one of them seriously.Under investigation.129

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 hydrogen130 and the storage of hydrogen. What follows is a list of some of the major codes and standards regulating hydrogen:

Name of standardShort title
29CFR1910.103Gaseous and cryogenic hydrogen handling and storage
29CFR1910.119Process safety management of highly hazardous chemicals
40CFR68Chemical accident prevention provisions
49CFRRegulations on shipping and handling hydrogen gas and cryogenic hydrogen131
ISO 13984:1999Liquid hydrogen — Land vehicle fuelling system interface
ISO/AWI 13984Liquid Hydrogen Land Vehicle Fueling Protocol
ISO/AWI 13985Liquid hydrogen — Land vehicle fuel tanks
ISO/CD 14687Hydrogen fuel quality — Product specification
ISO/AWI TR 15916Basic considerations for the safety of hydrogen systems
ISO 16110Hydrogen generators using fuel processing technologies
ISO 16111Transportable gas storage devices — Hydrogen absorbed in reversible metal hydride
ISO/AWI 17268Gaseous hydrogen land vehicle refuelling connection devices
ISO 19880Gaseous hydrogen — Fuelling stations
ISO/AWI 19881Gaseous hydrogen — Land vehicle fuel containers
ISO 19882Gaseous hydrogen — Thermally activated pressure relief devices for compressed hydrogen vehicle fuel containers
ISO/TS 19883Safety of pressure swing adsorption systems for hydrogen separation and purification
ISO/WD 19884Gaseous hydrogen — Cylinders and tubes for stationary storage
ISO/CD 19885Gaseous hydrogen — Fuelling protocols for hydrogen-fueled vehicles — Part 1: Design and development process for fueling protocols
ISO/CD 19887Gaseous Hydrogen — Fuel system components for hydrogen fuelled vehicles
ISO/AWI 22734Hydrogen generators using water electrolysis — Industrial, commercial, and residential applications
ISO/AWI 24078Hydrogen in energy systems — Vocabulary
ISO 26142:2010Hydrogen detection apparatus — Stationary applications132
NFPA 2Hydrogen technologies code
NFPA 30ARules for design of refueling stations
NFPA 50AStandard for gaseous hydrogen systems at consumer sites
NFPA 50BStandard for liquefied hydrogen systems at consumer sites
NFPA 52Compressed Natural Gas Vehicular Fuel Systems Code
NFPA 57Liquefied natural gas vehicular fuel systems standard133
CGA C-6.4Methods for External Visual Inspection of Natural Gas Vehicle (NGV) and Hydrogen Gas Vehicle (HGV) Fuel Containers and Their Installations
CGA G-5Hydrogen
CGA G-5.3Commodity Specification for Hydrogen
CGA G-5.4Standard for Hydrogen Piping Systems at User Locations
CGA G-5.5Hydrogen Vent Systems
CGA G-5.6Hydrogen Pipeline Systems
CGA G-5.7Carbon Monoxide and Syngas Pipeline Systems
CGA H-3Standard for Cryogenic Hydrogen Storage
CGA H-4Terminology Associated with Hydrogen Fuel Technologies
CGA H-5Standard for Bulk Hydrogen Supply Systems (an American National Standard)
CGA H-7Standard Procedures for Hydrogen Supply Systems
CGA H-10Combustion Safety for Steam Reformer Operation
CGA H-11Safe Startup and Shutdown Practices for Steam Reformers
CGA H-12Mechanical Integrity of Syngas Outlet Systems
CGA H-13Hydrogen Pressure Swing Adsorber (PSA) Mechanical Integrity Requirements
CGA H-14HYCO Plant Gas Leak Detection and Response Practices
CGA H-15Safe Catalyst Handling in HYCO Plants
CGA H-16Guideline on Remedial Actions for HYCO Plant Components Subject to High Temperature Hydrogen Attack
CGA P-6Standard Density Data, Atmospheric Gases and Hydrogen
CGA P-28OSHA Process Safety Management and EPA Risk Management Plan Guidance Document for Bulk Liquid Hydrogen Supply Systems
CGA P-74Standard for Tube Trailer Supply Systems at Customer Sites
CGA PS-31CGA Position Statement on Cleanliness for Proton Exchange Membranes Hydrogen Piping/Components
CGA PS-33CGA Position Statement on Use of LPG or Propane Tank as Compressed Hydrogen Storage Buffers
CGA PS-46CGA Position Statement on Roofs Over Hydrogen Storage Systems
CGA PS-48CGA Position Statement on Clarification of Existing Hydrogen Setback Distances and Development of New Hydrogen Setback Distances in NFPA 55
CGA PS-69CGA 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.134 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).135 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 136 and the Sourcebook for Hydrogen Applications.137138

Another organization responsible for hydrogen safety guidelines is the Compressed Gas Association (CGA), which has a number of references of their own covering general hydrogen storage,139 piping,140 and venting.141142

In 2023 CGA launched the 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

  1. "Hydrogen Safety" (PDF). Office of Energy Efficiency and Renewable Energy. https://www1.eere.energy.gov/hydrogenandfuelcells/pdfs/h2_safety_fsheet.pdf

  2. "Hydrogen Safety" (PDF). Office of Energy Efficiency and Renewable Energy. https://www1.eere.energy.gov/hydrogenandfuelcells/pdfs/h2_safety_fsheet.pdf

  3. Utgikar, Vivek P; Thiesen, Todd (2005). "Safety of compressed hydrogen fuel tanks: Leakage from stationary vehicles". Technology in Society. 27 (3): 315–320. doi:10.1016/j.techsoc.2005.04.005. /wiki/Doi_(identifier)

  4. Cadwallader, L. C.; Herring, J. S. (1999). Safety Issues with Hydrogen as a Vehicle Fuel (Technical report). doi:10.2172/761801. https://www.osti.gov/servlets/purl/761801

  5. "AIAA G-095-2004, Guide to Safety of Hydrogen and Hydrogen Systems" (PDF). AIAA. Retrieved 2008-07-28. http://aero-defense.ihs.com/document/abstract/GFEIHBAAAAAAAAAA

  6. "List of NFPA Codes & Standards". NFPA. https://www.nfpa.org/Codes-and-Standards/All-Codes-and-Standards/List-of-Codes-and-Standards

  7. "ISO/TC 197 – Hydrogen technologies". www.iso.org. https://www.iso.org/committee/54560/x/catalogue/p/1/u/1/w/0/d/0

  8. "Canadian Hydrogen Safety Program testing H2/CNG". Hydrogenandfuelcellsafety.info. Archived from the original on 2011-07-21. Retrieved 2010-07-05. https://web.archive.org/web/20110721205150/http://www.hydrogenandfuelcellsafety.info/2007/jun/h2cng.asp

  9. Utgikar, Vivek P.; Thiesen, Todd (2005). "Safety of compressed hydrogen fuel tanks: Leakage from stationary vehicles". Technology in Society. 27 (3): 315–320. doi:10.1016/j.techsoc.2005.04.005. /wiki/Doi_(identifier)

  10. "Hydrogen Safety" (PDF). Office of Energy Efficiency and Renewable Energy. https://www1.eere.energy.gov/hydrogenandfuelcells/pdfs/h2_safety_fsheet.pdf

  11. Lewis, Bernard; Guenther, von Elbe (1961). Combustion, Flames and Explosions of Gases (2nd ed.). New York: Academic Press, Inc. p. 535. ISBN 978-0124467507. {{cite book}}: ISBN / Date incompatibility (help) 978-0124467507

  12. Kalyanaraman, M (4 September 2019). "'Only a question of time' until large hydrogen systems are stable". Riviera Maritime Media. https://www.rivieramm.com/videos/how-tonbsp-hydrogen-fuel-cell-uptake-56079

  13. Barbalace, Kenneth. "Periodic Table of Elements - Hydrogen - H". http://environmentalchemistry.com/yogi/periodic/H.html#Physical

  14. Gregory, Frederick D. (February 12, 1997). "Safety Standard for Hydrogen and Hydrogen Systems" (PDF). NASA. Archived from the original (PDF) on February 27, 2006. Retrieved 2008-05-09. https://web.archive.org/web/20060227001252/http://www.hq.nasa.gov/office/codeq/doctree/canceled/871916.pdf

  15. MSHA – Safety Hazard Information – Special Hazards of Acetylene Archived 2016-01-22 at the Wayback Machine. Msha.gov. Retrieved on 2012-07-13. https://www.msha.gov/alerts/hazardsofacetylene.htm

  16. Sarah Eck & Michael D. Snyder (December 2021). "Hydrogen Safety Fundamentals". Chemical Engineering Progress: 36–41.

  17. "Use of "Quick-Disconnect" Fittings Results in Laboratory Instrument Explosion". H2Tools. Pacific Northwest National Laboratory. September 2017. https://h2tools.org/lessons/use-quick-disconnect-fittings-results-laboratory-instrument-explosion

  18. "Hydrogen Tube Trailer Explosion". H2Tools. Pacific Northwest National Laboratory. September 2017. https://h2tools.org/lessons/hydrogen-tube-trailer-explosion

  19. "Hydrogen Lab Fire". H2Tools. Pacific Northwest National Laboratory. September 2017. https://h2tools.org/lessons/hydrogen-lab-fire

  20. "Hydrogen Safety" (PDF). Office of Energy Efficiency and Renewable Energy. https://www1.eere.energy.gov/hydrogenandfuelcells/pdfs/h2_safety_fsheet.pdf

  21. Lewis, Bernard; Guenther, von Elbe (1961). Combustion, Flames and Explosions of Gases (2nd ed.). New York: Academic Press, Inc. p. 535. ISBN 978-0124467507. {{cite book}}: ISBN / Date incompatibility (help) 978-0124467507

  22. "Fire at Hydrogen Fueling Station". H2Tools. Pacific Northwest National Laboratory. September 2017. The initial source of fire was likely a release of hydrogen from a failed weld on a pressure switch. https://h2tools.org/lessons/fire-hydrogen-fueling-station

  23. "Small Fire in Fule Cell Test Stand". H2Tools. Pacific Northwest National Laboratory. September 2017. An electrical short circuit occurred, causing a small electrical fire. https://h2tools.org/lessons/small-fire-fuel-cell-test-stand

  24. "Incorrect Relief Valve Set Point Leads to Explosion". H2Tools. Pacific Northwest National Laboratory. September 2017. Contributing cause was poor design of the venting system, which was installed in a horizontal position, causing inadequate venting and buildup of static electricity. https://h2tools.org/lessons/incorrect-relief-valve-set-point-leads-explosion

  25. "Fuel Cell Evaporation Pad Fire". H2Tools. Pacific Northwest National Laboratory. September 2017. 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. https://h2tools.org/lessons/fuel-cell-evaporator-pad-fire

  26. Sarah Eck & Michael D. Snyder (December 2021). "Hydrogen Safety Fundamentals". Chemical Engineering Progress: 36–41.

  27. "Hydrogen Explosion Due to Inadequate Maintenance". H2Tools. Pacific Northwest National Laboratory. September 2017. 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. https://h2tools.org/lessons/hydrogen-explosion-due-inadequate-maintenance

  28. "Hydrogen Explosion at Coal-Fired Power Plant". H2Tools. Pacific Northwest National Laboratory. September 2017. Explore elimination of rupture disk PRDs and substitution of spring-style relief valves. https://h2tools.org/lessons/hydrogen-explosion-coal-fired-power-plant

  29. Abderholden, Frank S. (18 December 2019). "Waukegan plant explosion that killed four workers was preventable, federal officials say". chicagotribune.com. Retrieved 2020-01-06. 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. https://www.chicagotribune.com/suburbs/lake-county-news-sun/ct-lns-waukegan-blast-safety-update-st-1219-20191218-2hp6o6hyxrc6df6b6lr6xwdjge-story.html

  30. Japanese engineers work to contain nuclear reactor damage, Los Angeles Times, March 14, 2011 http://www.latimes.com/news/science/la-sci-japan-quake-reactor-qa-20110314,0,5470584.story

  31. Chernobyl Accident Appendix 1: Sequence of Events Archived 2016-01-14 at the Wayback Machine, World Nuclear Association, November 2009 http://www.world-nuclear.org/info/Safety-and-Security/Safety-of-Plants/Appendices/Chernobyl-Accident---Appendix-1--Sequence-of-Events/

  32. Gregory, Frederick D. (February 12, 1997). "Safety Standard for Hydrogen and Hydrogen Systems" (PDF). NASA. Archived from the original (PDF) on February 27, 2006. Retrieved 2008-05-09. https://web.archive.org/web/20060227001252/http://www.hq.nasa.gov/office/codeq/doctree/canceled/871916.pdf

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  34. "Gaseous Hydrogen Leak and Explosion". H2Tools. Pacific Northwest National Laboratory. September 2017. 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. https://h2tools.org/lessons/gaseous-hydrogen-leak-and-explosion

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