By John Spouge
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2. Is piping designed for the maximum shut-in pressure of any input source or adequately protected per API RP14C? 3. Do all SDVs fail in the safe position? 4. Are pipeline riser SDVs or FSVs located below the lowest process level if practical? 5. Have relief and vent systems (if any) been determined to be adequately sized and properly located? 6. Are there adequate start-up, operations, shutdown, maintenance, inspection and testing programs and procedures in place? 7. Are there any unusual materials, equipment or circumstances that may require additional review?
International Symposia on Loss Prevention and Safety Promotion in the Process Industries, organised by the European Federation of Chemical Engineering (every 2-3 years) - covers onshore and offshore process safety. - UK Institution of Chemical Engineers Symposium Series (1-2 per year) - covers various subjects including onshore and offshore process safety. - Risk Analysis in the Offshore Industry, organised by IBC (annual) - a conference with emphasis on training. - Offshore Technology Conference (annual) - comprehensive coverage of offshore technology, with some safety aspects.
The technique has been used extensively in Norway, and the term ‘CSE’ has been adopted world-wide, although in reality it normally refers to a QRA during the concept stage (often a fatality risk assessment) rather than the NPD methodology. Pyman & Gjerstad (1983) describe an early CSE. The NPD methodology for CSEs makes one major simplification compared to many other QRAs - it does not consider the risk of fatalities but the risk of impairment of safety functions. The safety functions are: • Escape routes • Shelter areas (usually the living quarters) • Main support structure of the platform It makes what is in general a reasonable assumption - that the lower the frequency of accidents that impair these safety functions, the more acceptable the concept design is.