Synergy of CO2 removal and light hydrocarbon recovery from oil-field associated gas by dual-membrane process

被引:18
作者
Chen, Bo [1 ]
Ruan, Xuehua [2 ]
Xiao, Wu [1 ]
Jiang, Xiaobin [1 ]
He, Gaohong [1 ,2 ]
机构
[1] Dalian Univ Technol, Sch Chem Engn, Res & Dev Ctr Membrane Sci & Technol, State Key Lab Fine Chem, Dalian 116024, Peoples R China
[2] Dalian Univ Technol, Sch Petr & Chem Engn, Res & Dev Ctr Membrane Sci & Technol, State Key Lab Fine Chem, Dalian 116024, Peoples R China
基金
中国国家自然科学基金;
关键词
Process intensification; Dual-membrane module; Gas separation; Oil-field associated gas; Light hydrocarbon recovery; HOLLOW-FIBER MEMBRANE; NATURAL-GAS; CARBON-DIOXIDE; POLYMERIC MEMBRANES; PROCESS DESIGN; SEPARATION; PERMEATION; PERFORMANCE; MIXTURES; CAPTURE;
D O I
10.1016/j.jngse.2015.08.028
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
CO2 enhanced oil recovery technology is widely used in depleted oil-fields; however, the CO2 content in the associated gases is increased accordingly, which is unfavorable for both light hydrocarbon recovery and natural gas purification. This work proposes a dual-membrane associated gas recovery process, which couples hydrocarbon separation and CO2 removal in the dual-membrane modules and improves the process efficiency. The dual-membrane module contains both hydrocarbon-selective and CO2-selective membranes, enabling the hydrocarbons and CO2 to be recovered from bulk flow separately and simultaneously. The hydrocarbons are enriched in the permeate side of the hydrocarbon-selective membrane, and the permeate stream is re-pressurized for recovering valuable hydrocarbons. Meanwhile, CO2 is concentrated in the permeate side of CO2-selective membrane for enhanced oil recovery usage. The synergetic separation in the dual-membrane module significantly reduces the hydrocarbon loss while removing CO2, and results in higher hydrocarbon recovery than the single-membrane process or series-linked membrane process. The production cost savings of the dual-membrane module process are greater than 9%, because of the mutual promotion of hydrocarbon enrichment and CO2 removal by the dual-membrane module. (C) 2015 Published by Elsevier B.V.
引用
收藏
页码:1254 / 1263
页数:10
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