Event
- Event ID
- 289
- Quality
- Description
- A hydrogen explosion occurred in a 5-tonne stainless steel pressure vessel, while two electro-polisher workers where electropolishing internal surfaces. The reason of the explosion was possibly the build-up a hydrogen - oxygen mixture within the vessel of, generated by the electropolishing process.
The vessel laid horizontally with the only one unsealed opening: a man-way in the front-end site. There were no measure aiming at evacuating the gasses generated within vessel, and/or at avoiding sources of ignition. Significant quantities of hydrogen were likely generated due to the attempt to electropolishing the vessel using large cathode / anode area and high energy input. The vessel was approximately half full with concentrated (sulphuric / phosphoric) acid.
The explosion resulted in injuries, a fatality and in the ejection of a substantial quantities of the acid. - Event Initiating system
- Classification of the physical effects
- Hydrogen Release and Ignition
- Nature of the consequences
- Macro-region
- Europe
- Country
- United Kingdom
- Date
- Main component involved?
- Chemical Storage Tank
- How was it involved?
- Internal Explosion (H2-O2 Mixture)
- Initiating cause
- Accidental Hydrogen Formation
- Root causes
- Root CAUSE analysis
- The INITIATING cause was the accidental production of a hydrogen-oxygen mixture while electroplating.
A CONTRIBUTING CAUSE was that this was the first such job undertaken by those injured, inexperience and failure to identify risk played a role
The ROOT CAUSE is management shortcoming. Industrial standard were available but not applied. The workers had not knowledge of the hazards involved and there was no mitigating/preventive measure.
Facility
- Application
- Steel And Metals Industry
- Sub-application
- Steel manufacturing
- Hydrogen supply chain stage
- All components affected
- Pressure vessel for chemical storage
- Location type
- Confined
- Location description
- Industrial Area
- Operational condition
- Pre-event occurrences
- Maintenance works (electropolishing) were ongoing.
Emergency & Consequences
- Number of injured persons
- 1
- Number of fatalities
- 1
- Post-event summary
- The explosion resulted in one injured and one fatality and in the ejection of a substantial quantities of the acid.
- Official legal action
- The event was investigated by HSE UK.
- Investigation comments
- The following comments were recorded by the inspector:
Industry standard for treatment of such vessels appears to be to:
1) Electro-polish end caps prior to assembly and then to electro-polish internal circumference with the vessel continually rotated on powered rollers and with a cathode hung from centres into a small volume of electrolyte in the base of the vessel
2) Evacuate generated gases by feeding air into vessel and / or providing extraction.
Vessel involved in accident was first such job undertaken by those injured - inexperience and failure to identify risk are considered to be the main underlying causes. - Emergency action
- 1. September 25: Completed inspection
2. September 28: Start of operation
3. October 5: During hydrogen fueling to the 4th vehicle (10th since the start of operation) (Temperature: -37°C, Pressure: 63 MPa), the hydrogen gas leak detection alarm device inside the dispenser activated. After detecting the leak, the hydrogen inside the piping was automatically depressurized and released from the vent. The leakage point was investigated using a portable hydrogen gas detector, but it was not identified. (This is a separate hydrogen leakage accident from the one mentioned above.)
4. October 6: Under the supervision of the equipment manufacturer, the leakage point was thoroughly investigated, and it was confirmed that the shut-off valve inside the dispenser was leaking.
5. October 6: The O-ring of the shut-off valve inside the dispenser was replaced, and during the hydrogen fueling test to a fuel cell vehicle (Temperature: -37°C, Pressure: 55 MPa), the hydrogen gas leak detection alarm device inside the dispenser activated. The leakage point was investigated using a portable hydrogen gas detector, and it was confirmed that the lower part of the emergency disconnect coupler on the fueling nozzle side of the fueling hose was leaking.
Lesson Learnt
- Lesson Learnt
- It was the first time that the workers executed the process which brought to the incident. Inexperience and failure to identify risk are considered to be the main underlying causes. There were standard practice in place. The industry standard for treatment of such vessels appears to be to:
1) electropolishing end caps prior to assembly and then to electropolishing internal circumference with the vessel continually rotated on powered rollers and with a cathode hung from centres into a small volume of electrolyte in the base of the vessel
2) evacuate generated gases by feeding air into vessel and / or providing extraction.
None of these steps were undertaken and no preventing measure was put in place.
Event Nature
- Release type
- gas
- Involved substances (% vol)
- H2 100%
- Presumed ignition source
- Electricity
- Deflagration
- N
- High pressure explosion
- N
- High voltage explosion
- N
References
- Reference & weblink
Event description provided by HSE, original source confidential
JRC assessment
- Sources categories
- HSE