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A CFD based explosion risk analysis methodology using time varying release rates in dispersion simulations
Institution:1. Centre for Offshore Engineering and Safety Technology, China University of Petroleum, Qingdao, 266580, China;2. Centre for Risk, Integrity and Safety Engineering (C-RISE), Faculty of Engineering and Applied Science, Memorial University of Newfoundland, St. John’s, NL, A1B 3X5, Canada;1. Department of Chemical Engineering, Tarbiat Modares University (TMU), Jalal Al Ahmad Highway, Tehran, Iran;2. Development & Engineering Management Department, South Pars Gas Complex Company, Assaluyeh, Iran;3. Young Researchers and Elite Club, Robatkarim Branch, Islamic Azad University, Robatkarim, Iran;1. Center for Offshore Engineering and Safety Technology, China University of Petroleum, Qingdao, 266580, China;2. Centre for Risk, Integrity and Safety Engineering (C-RISE), Faculty of Engineering and Applied Science, Memorial University of Newfoundland, St. John''s, NL, A1B 3X5, Canada;3. Centre for Infrastructural Monitoring and Protection, School of Civil and Mechanical Engineering, Curtin University, WA, 6102, Australia;1. Center for Offshore Engineering and Safety Technology, China University of Petroleum, Qingdao 266580, China;2. Tianjin University-Curtin University Joint Research Centre of Structure Monitoring and Protection, School of Civil and Mechanical Engineering, Curtin University, WA 6102, Australia
Abstract:A full probabilistic Explosion Risk Analysis (ERA) is commonly used to establish overpressure exceedance curves for offshore facilities. This involves modelling a large number of gas dispersion and explosion scenarios. Capturing the time dependant build up and decay of a flammable gas cloud size along with its shape and location are important parameters that can govern the results of an ERA. Dispersion simulations using Computational Fluid Dynamics (CFD) are generally carried out in detailed ERA studies to obtain these pieces of information. However, these dispersion simulations are typically modelled with constant release rates leading to steady state results. The basic assumption used here is that the flammable gas cloud build up rate from these constant release rate dispersion simulations would mimic the actual transient cloud build up rate from a time varying release rate. This assumption does not correctly capture the physical phenomena of transient gas releases and their subsequent dispersion and may lead to very conservative results. This in turn results in potential over design of facilities with implications on time, materials and cost of a project.In the current work, an ERA methodology is proposed that uses time varying release rates as an input in the CFD dispersion simulations to obtain the fully transient flammable gas cloud build-up and decay, while ensuring the total time required to perform the ERA study is also reduced. It was found that the proposed ERA methodology leads to improved accuracy in dispersion results, steeper overpressure exceedance curves and a significant reduction in the Design Accidental Load (DAL) values whilst still maintaining some conservatism and also reducing the total time required to perform an ERA study.
Keywords:Explosion risk analysis  CFD  Time varying release rate  Fully transient Q9  Explosion overpressure  Cost-effective blast protection  ACH"}  {"#name":"keyword"  "$":{"id":"kwrd0045"}  "$$":[{"#name":"text"  "_":"air changes per hour  CFD"}  {"#name":"keyword"  "$":{"id":"kwrd0055"}  "$$":[{"#name":"text"  "_":"computational fluid dynamics  DAL"}  {"#name":"keyword"  "$":{"id":"kwrd0065"}  "$$":[{"#name":"text"  "_":"design accidental load  ERA"}  {"#name":"keyword"  "$":{"id":"kwrd0075"}  "$$":[{"#name":"text"  "_":"explosion risk analysis  FLACS"}  {"#name":"keyword"  "$":{"id":"kwrd0085"}  "$$":[{"#name":"text"  "_":"FLame ACceleration Simulator  FPSO"}  {"#name":"keyword"  "$":{"id":"kwrd0095"}  "$$":[{"#name":"text"  "_":"floating production  storage and offloading  HSE"}  {"#name":"keyword"  "$":{"id":"kwrd0105"}  "$$":[{"#name":"text"  "_":"health and safety executive  UK  IFBF"}  {"#name":"keyword"  "$":{"id":"kwrd0115"}  "$$":[{"#name":"text"  "_":"isolation failure and blowdown failure  ISBS"}  {"#name":"keyword"  "$":{"id":"kwrd0125"}  "$$":[{"#name":"text"  "_":"isolation success and blowdown success  LFL"}  {"#name":"keyword"  "$":{"id":"kwrd0135"}  "$$":[{"#name":"text"  "_":"lower flammability limit  NORSOK"}  {"#name":"keyword"  "$":{"id":"kwrd0145"}  "$$":[{"#name":"text"  "_":"“Norsk Sokkels Konkurranseposisjon”  the Norwegian initiative to reduce cost on offshore projects  Q6"}  {"#name":"keyword"  "$":{"id":"kwrd0155"}  "$$":[{"#name":"text"  "_":"increase in flammable cloud volume in each time step (FLACS parameter)  Q9"}  {"#name":"keyword"  "$":{"id":"kwrd0165"}  "$$":[{"#name":"text"  "_":"equivalent stoichiometric cloud volume (FLACS parameter)  TDIIM"}  {"#name":"keyword"  "$":{"id":"kwrd0175"}  "$$":[{"#name":"text"  "_":"time dependant internal ignition model  UFL"}  {"#name":"keyword"  "$":{"id":"kwrd0185"}  "$$":[{"#name":"text"  "_":"upper flammability limit
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