Submitted:
20 July 2023
Posted:
20 July 2023
You are already at the latest version
Abstract
Keywords:
1. Introduction
1.1. Prospect and Limitation of Hydrogen Energy in Terms of Aging
1.2. Historical Scenario of Hydrogen-Induced Aging
1.3. Impact of Operating Conditions on Hydrogen-Assisted Aging
1.4. Potential Reasons of Hydrogen Assisted Aging
1.5. Potential Mechanism of Hydrogen-Induced Aging on Storage and Sealing Materials
2. Methods of Aging in a Hydrogen Environment
2.1. Thermal Aging
2.1.1. Mechanism of Thermal Aging
2.1.2. Laboratory Test for Thermal Aging
2.2. Chemical Aging
2.2.1. Mechanism of Chemical Aging
2.2.2. Laboratory Test for Chemical Aging
2.3. Mechanical Aging
2.3.1. Mechanism of Mechanical Aging
2.3.2. Laboratory Test for Mechanical Aging
2.4. Mechanical-Chemical Aging
2.4.1. Mechanism of Mechanical-Chemical Aging
2.4.2. Laboratory Test for Mechanical-Chemical Aging
2.5. Thermo-Mechanical Aging
2.5.1. Mechanism of Thermo-Mechanical Aging
2.5.2. Laboratory Test for Thermo-Mechanical Aging
3. Durability Analysis of Hydrogen Sealing and Storage Materials through Aging Tests
3.1. Durability Test Methods and Principles
3.2. Service Life of Storage and Sealing Material under Simultaneous Multiple Aging
4. Key Factors Affecting Aging under the Hydrogen Environment
4.1. Effects of Temperature
4.2. Effect of Pressure
4.3. Effects of Stress
4.4. Effects of Thermal Cycle
4.5. Effects of Environment
4.6. Effects of Alloying Elements
5. Research Gap Analysis
6. Conclusion
Author Contributions
Funding
Conflicts of Interest
References
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| Hydrogen | Natural gas | Petrol | |
|---|---|---|---|
| Energy content per unit mass | 120.4 MJ/kg | 51.6 MJ/kg | 43 MJ/kg |
| Energy content per unit volume | 480 MJ/Gallon | 180 MJ/Gallon | 120 MJ/Gallon |
| Incident | Cause | Reference |
|---|---|---|
| The Flixborough disaster was a chemical plant explosion that was taken place at Flixborough, North Lincolnshire, England on 1 June 1974. Here, 28 people were killed, and 36 were seriously injured, among 72 people. | The chemical plant had a cyclohexane plant, and the incident was introduced from there. The reactor circuit leaked due to the aging, and a huge hydrocarbon gas cloud was formed, which eventually led to an explosion by an ignition source from a furnace nearby a hydrogen production plant. | [10] |
| The Humber Refinery explosion was taken place at South Killingholme in North Lincolnshire, England, on 16 April 2001. Here, two people were injured, but the scenario could be more dangerous if the day did not become a holiday. | Steel pipe failure was the main reason behind the explosion. The steel pipe was coated with a passive layer of iron sulfide which was protecting it from corrosion. But due to the aging, the protecting layer was ruptured, and the pipe surface was exposed to corrosion. As a result, the thickness of the pipe was reduced to 0.3 mm from 7-8 mm, which could not contain the internal pressure and burst. | [11] |
| The Chevron refinery accident was taken place in Richmond, California, on 06 August 2012. | The main reason for this accident was the wall thinning of the pipe due to aging, which led to a catastrophic pipe rupture. | [12] |
| A fetal hydrogen explosion at a power plant in Muskingum, Ohio in 2007. | The disaster began with the premature failure of the rupture disk on the storage tank as a result of aging. The pressurized gas then caused the vent system to fail, allowing hydrogen to escape and causing an explosion. | [13] |
| Tesoro refinery explosion in Anacortes, Washington, USA in 2010. | The accident was the result of damage to the heat exchanger brought on by hydrogen aging at high temperatures, which led to carbon steel tubing being badly fractured and weakened, which in turn led to a rupture. | [14] |
| The 1982 explosion at Kashima Oil Refinery in Japan. | The explosion was caused by hydrogen aging under high pressure and high pressure in a hydrodesulfurization unit. Five casualties were caused by the gradual deterioration of the inner surface of a carbon steel pipe, which resulted in the discharge of process fluid after 12 years of operation. | [15] |
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