A Novel Process for Natural Gas Liquids Recovery from Oil Field Associated Gas with Liquefied Natural Gas Cryogenic Energy Utilization
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A Novel Process for Natural Gas Liquids Recovery from Oil Field Associated Gas with Liquefied Natural Gas Cryogenic Energy Utilization
A Novel Process for Natural Gas Liquids Recovery from Oil Field Associated Gas with Liquefied Natural Gas Cryogenic Energy Utilization
中国化学工程学报(英文版)2011年19卷第3期 页码:452-461
Affiliations:
School of Chemistry and Chemical Engineering, the State Key Lab for Pulp and Paper Engineering, South China University of Technology,Guangzhou,China,510640
Author bio:
Funds:
Supported by the National Natural Science Foundation of China(20876056,20536020);the PhD Program Fund from Ministry of Education of China(20100172110016)
边海军, 徐文东, 李秀喜, 等. A Novel Process for Natural Gas Liquids Recovery from Oil Field Associated Gas with Liquefied Natural Gas Cryogenic Energy Utilization[J]. 中国化学工程学报(英文版), 2011,19(3):452-461.
BIAN Haijun, XU Wendong, LI Xiuxi, QIAN Yu. A Novel Process for Natural Gas Liquids Recovery from Oil Field Associated Gas with Liquefied Natural Gas Cryogenic Energy Utilization[J]. , 2011, 19(3): 452-461.
边海军, 徐文东, 李秀喜, 等. A Novel Process for Natural Gas Liquids Recovery from Oil Field Associated Gas with Liquefied Natural Gas Cryogenic Energy Utilization[J]. 中国化学工程学报(英文版), 2011,19(3):452-461.DOI: 10.1016/S1004-9541(11)60006-2.
BIAN Haijun, XU Wendong, LI Xiuxi, QIAN Yu. A Novel Process for Natural Gas Liquids Recovery from Oil Field Associated Gas with Liquefied Natural Gas Cryogenic Energy Utilization[J]. , 2011, 19(3): 452-461.DOI: 10.1016/S1004-9541(11)60006-2.
A Novel Process for Natural Gas Liquids Recovery from Oil Field Associated Gas with Liquefied Natural Gas Cryogenic Energy Utilization
A novel process to recovery natural gas liquids from oil field associated gas with liquefied natural gas (LNG)cryogenic energy utilization is proposed.Compared to the current electric refrigeration process
the proposed process uses the cryogenic energy of LNG and saves 62.6%of electricity.The proposed process recovers ethane
liquid petroleum gas(propane and butane)and heavier hydrocarbons
with total recovery rate of natural gas liquids up to 96.8%.In this paper
exergy analysis and the energy utilization diagram method(EUD)are used to assess the new process and identify the key operation units with large exergy loss.The results show that exergy efficiency of the new process is 44.3%.Compared to the electric refrigeration process
exergy efficiency of the new process is improved by 16%.The proposed process has been applied and implemented in a conceptual design scheme of the cryogenic energy utilization for a 300 million tons/yr LNG receiving terminal in a northern Chinese harbor.
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