When all the dominos fall against you
The 2015 Unipetrol Litvínov ethylene unit incident
It is nine years since the explosion and fires at the Unipetrol Litvínov ethylene unit at Chempark Zaluzi in the Czech Republic on 13 August 2015.? It was a telling example of a ‘chain reaction’ or ‘domino effect’ incident, where the initial incident caused a second incident, which caused a third incident, and beyond.
Two operators went to changeover the cooling water supply to the Light Ends of the ethylene unit, switching from the normally operating pipeline (3) to the parallel spare pipeline (4), in order to perform a regular calibration of the flowmeter on line 3.? To do so the flow on 4 would be established by opening the inlet and outlet block valves around its flowmeter, before shutting off the flow on 3.? Well, you can probably guess where this is heading.??
As is often the case with identical process equipment, a simple mistake was made.? After opening the outlet block valve on 4, the Operator closed the outlet block valve on 3, rather than opening the inlet on 4, thus stopping the cooling water flow to the Light Ends.? This set off a pretty remarkable chain of events;
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They say that from tiny seeds grow mighty trees.? Unfortunately, massive incidents sometimes arise from the smallest error.? The fires took almost 24 hours to put out, with 499 firefighters attending the site.? This incident kept the ethylene unit offline for just over 14 months whilst four furnaces were fully replaced and a major repairs were made to much of the rest of the unit.
Fault tolerant systems are designed with the presumption that humans will make mistakes.? Even the most experienced operator is fallible.? Valve switchover procedures are notorious for being done incorrectly and leading to major incidents (Williams Geismar 2013, Jaipur 2009).? Trapped key interlocking systems (e.g. Castell Interlock) are one way to prevent this by making valves physically inoperable unless manipulated in the correct sequence.??
At the time I remember it reignited a periodic debate amongst Energy Risk Professionals about the concept of double jeopardy i.e. should the scenarios used for loss estimates consider secondary (and even tertiary) knock-on incidents.? That old chestnut will be argued forever without resolution, but what the Litvínov incident did contribute to the debate was the fact that hidden within the sprawling oil, gas and petrochemical facilities that we survey are many ‘nodes’ where an escalation vector is baked in.??
We can’t identify them all, and the Insured can’t realistically be expected to engineer them all away.? But one thing which Energy Risk Professionals excel at is identifying under-appreciated exposures that create major risks, and then providing practical recommendations for how to remove those gaps.? There were four open insurance survey recommendations at Unipetrol Litvínov prior to the incident which - if they had been resolved - may have stopped the escalation sequence...
An overview video summarising the incident was made by Unipetrol and is available here.
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6 个月Great lesson!!!! An important reflection is to consider the potential errors of the operators and the risk studies must start from the first phases of the design; in the detailed engineering phase there is already greater resistance to adding risk engineering controls such as the sequential valves not initially budgeted in the project; even so, the facilitator and the team of the last risk studies must not overlook these potential scenarios.
Safety Consultant
6 个月While I guess fitting pilot operated safety valves would be the best solution to help minimise s/v chatter, would there any merit in fitting longer studs to allow double nutting? So the second nut acts as a lock nut to the first one, similar in theory to removing a stud from an engine casing using two nuts.
Process Engineer | IChemE Australia Chair
6 个月Thanks for sharing Ryan. I happened upon this one recently via the 100 Largest Losses. Quite an escalation and it’s good that Unipetrol have been so open with sharing their lessons learned.
Process Safety & Loss Prevention Engineer | Functional Safety Professional | Experienced in HAZOP, LOPA, SIL Assessment, Bowtie, QRA, Fire Protection, F&G Mapping | Former Ammonia Plant Engineer
6 个月Thank you so much for sharing the detailed analysis. The best operator can come up with a very unusual mistake and that is what is most debated in risk studies and the usual comment "This has never happened" & that's why it's imperative not to consider the operator at his best during risk studies. From cooling water failure to PSV lift , there must have been alarms ringing for the panel operator and clearly there must have been a communication gap between the field and the panel operator.