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强化采油伴生气捕碳及轻烃回收工艺模拟

Simulation on recovery of light hydrocarbon and CO2 capture from EOR-associated gas by PSA processes

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【作者】 刘冰安亚雄江南汪亚燕邢瑞张东辉徐铖君

【Author】 LIU Bing;AN Ya-xiong;JIANG Nan;WANG Ya-yan;XING Rui;ZHANG Dong-hui;XU Cheng-jun;State Key Laboratory of Chemical Engineering, Chemical Engineering Research Center, School of Chemical Engineering and Technology, Tianjin University;Investment Engineering Office of Fujian Sales Branch of China National Petroleum Corporation;

【通讯作者】 张东辉;

【机构】 天津大学化工学院化学工程研究所化学工程联合国家重点实验室中国石油天然气股份有限公司福建销售分公司投资工程处

【摘要】 针对气驱强化采油(EOR)过程所产生的低品质伴生气,提出以4A分子筛和活性炭为吸附剂,通过变压吸附法(PSA)进行分离,回收部分轻烃,捕碳返注地下的工艺。通过实验测定吸附剂的参数,建立上述工艺的数学模型,完成动态模拟。模拟结果表明:第1阶处理后,轻产品气中烃类纯度为64.37%;第2阶处理后,轻产品气中轻烃含量为64.35%;工艺的二氧化碳回收率为90.79%,轻烃回收率为70.67%,具有良好的环境效益。

【Abstract】 Enhanced oil recovery(EOR) process might release some low-quality associated gas. 4 A molecular sieve(4 A) and activated carbon(AC) were used as adsorbents for separation by two-stage vacuum pressure swing adsorption(VPSA). Isotherm of adsorbents was determined and calculated, and mathematical models were established. The simulation results show that the purity of hydrocarbons in light product gas is 64.37% after the first stage treatment, while that of the second stage is 64.35%. The recovery of CO2 is 90.79%, and that of light hydrocarbon is 70.67%, which shows environmental and economic benefits.

  • 【文献出处】 高校化学工程学报 ,Journal of Chemical Engineering of Chinese Universities , 编辑部邮箱 ,2020年02期
  • 【分类号】X741
  • 【被引频次】1
  • 【下载频次】135
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