search.noResults

search.searching

saml.title
dataCollection.invalidEmail
note.createNoteMessage

search.noResults

search.searching

orderForm.title

orderForm.productCode
orderForm.description
orderForm.quantity
orderForm.itemPrice
orderForm.price
orderForm.totalPrice
orderForm.deliveryDetails.billingAddress
orderForm.deliveryDetails.deliveryAddress
orderForm.noItems
OPERATIONS & MAINTENANCE


HYDROGEN SAFETY


A look at safety risks and solutions around hydrogen manufacturing


C


apitalising on the immense benefi ts of hydrogen as a green energy source requires several processes including


its production, storage, transportation and usage. Each of these stages required to realise the advantages of hydrogen energy also pose safety challenges that must be addressed in accordance with the unique properties of hydrogen and hydrogen production.


PROCESS HAZARD ANALYSIS For any new or existing hydrogen production applications, a Process Hazard Analysis (PHA) can help assess any potential risks associated with the various stages of hydrogen manufacturing and usage. At the conclusion of the PHA, a risk assessment report will be created and may identify the following at-risk areas and their potential solutions:


OVERPRESSURE HAZARDS Pressurised hydrogen exists throughout the creation, storage, transport and usage of hydrogen. Without a reliable means of pressure relief, a vessel can fracture and even result in a pressure-related explosion. To relieve excess pressure and


prevent catastrophic failure of the containment system, two methods of pressure relief are used: pressure relief valves (PRVs) and rupture discs. PRVs gently open and close as pressure fl uctuates, while rupture discs ‘burst’ when pressure reaches a certain undesirable level. While both devices provide reliable


pressure relief, it’s a common practice to use both PRVs and rupture discs in tandem with one another. For example, by installing a rupture disc upstream of a PRV, unwanted leakage of valuable product is avoided, as the


20 www.engineerlive.com


Reliable pressure relief and fi re detection prevent fractures and undetected fi res


hydrogen will only reach the PRV if the rupture disc opens.


FIRE HAZARDS Because hydrogen fi res are invisible, traditional fi re detection methods that rely on visible fl ames or smoke are ineff ective and unreliable. That’s why fl ame detectors with infrared technology are recommended to identify the thermal energy produced by hydrogen fi res allowing for quick emergency response, mitigation measures and system shutdown. Some fl ame detectors also include


an on-board camera that visualises the exact location of the hydrogen fl ame on a connected monitor to protect nearby workers and direct safety personnel.


EXPLOSION HAZARDS Owing to the wide fl ammability range and low ignition energy of hydrogen gas, explosive atmospheres are common in these applications. Explosion vents are a commonly used protection strategy that, like rupture discs, open when a specifi c pressure is reached to safely relieve the pressure and redirect fl ames away from people and other critical areas.


‘Flameless’ devices may also be used


to make explosion venting of indoor applications possible as they suppress the fl ames while allowing pressure to pass through.


CONCLUSION The various stages of hydrogen production each involve their own unique equipment and processes, and it is therefore essential for managers to partner with an expert in hydrogen safety who understands all the potential hazards and solutions. Conducting a PHA is almost


always a necessary fi rst step, it will help document any possible risks and provide a better understanding of areas that should be further investigated as well as those that are safe from the aforementioned hazards. The safety solutions provider should then work with the client to methodically reduce the risk of each of those hazard areas with recommended process improvements or required safety systems.


For more information visit: www.fi ke.com


Page 1  |  Page 2  |  Page 3  |  Page 4  |  Page 5  |  Page 6  |  Page 7  |  Page 8  |  Page 9  |  Page 10  |  Page 11  |  Page 12  |  Page 13  |  Page 14  |  Page 15  |  Page 16  |  Page 17  |  Page 18  |  Page 19  |  Page 20  |  Page 21  |  Page 22  |  Page 23  |  Page 24  |  Page 25  |  Page 26  |  Page 27  |  Page 28  |  Page 29  |  Page 30  |  Page 31  |  Page 32  |  Page 33  |  Page 34  |  Page 35  |  Page 36  |  Page 37  |  Page 38  |  Page 39  |  Page 40  |  Page 41  |  Page 42  |  Page 43  |  Page 44  |  Page 45  |  Page 46  |  Page 47  |  Page 48  |  Page 49  |  Page 50  |  Page 51  |  Page 52  |  Page 53  |  Page 54  |  Page 55  |  Page 56