China Safety Science Journal ›› 2021, Vol. 31 ›› Issue (12): 95-105.doi: 10.16265/j.cnki.issn 1003-3033.2021.12.013

• Safety engineering technology • Previous Articles     Next Articles

Risk analysis of oil and gas recovery process based on HAZOP-Aspen

LIU Shangzhi1, LI Hongbin1, ZHAO Dongfeng2,3, LIU Qinglong2, JIU Jiangbo2, MOU Rui1   

  1. 1 College of Mechanical and Electronic Engineering, China University of Petroleum, Qingdao Shandong 266580, China;
    2 Qingdao Oasis Environment & Safety Technology Co., Ltd., Qingdao Shandong 266580, China;
    3 College of Chemical Engineering, China University of Petroleum, Qingdao Shandong 266580, China
  • Received:2021-09-14 Revised:2021-11-12 Online:2021-12-28 Published:2022-06-28

Abstract: In order to evaluate inherent safety of oil and gas recovery process, a safety evaluation model was constructed based on HAZOP-Aspen considering characteristics of the process, including its simplicity, wide range of operating conditions and discontinuous operating conditions. Firstly, risks of the process were analyzed and main accident types were determined by adopting HAZOP. Then, based on Aspen procedure simulation, inherent safety was evaluated by a combined use of logistics index method and quantitative risk analysis. Finally, with typical "condensation + membrane separation" method as an example, the evaluation model was applied. The results show that the higher feed oil and gas concentration is, the lower inherent safety will be. The explosion limit of oil and gas is generally in the range of 2%-10%, and as concentration of feed oil and gas decreases, that of these in process stream will be closer to upper explosion range.

Key words: oil-gas recovery process, hazard and operability analysis (HAZOP), Aspen, process simulation, inherent safety, process stream index (PSI)

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