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Clean Hydrogen Partnership

Hydrogen accidentally produced by electropolishing

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