[1]郑伟林.单泵同心双管分层注聚工艺的理论分析及应用[J].西安石油学报:自然科学版,2010,25(3):41-45.
Zheng Weilin.Theoretical study and application of the concentric double-pipe layered polymer injection with single pump[J].Journal of Xi’an Shiyou University:Natural Science Edition,2010,25(3):41-45.
[2]贾庆生.液控式同心双管分层注水技术[J].石油机械,2009, 37(9):59-64.
Jia Qingsheng.Research on the technology of separate layer water injection by concentric double-tubing with hydraulic control packers[J].China Petroleum Machinery,2009,37(9):59-64.
[3]Chiu K,Thakur S C.Modeling of wellbore heat losses in directional wells under changing injection conditions[R].SPE 22870,1991.
[4]张小宁,李根生,黄中伟,等.泡沫钻井液在井筒中的流动与传热[J].石油学报,2010,31(1):134-138.
Zhang Xiaoning,Li Gensheng,Huang Zhongwei,et al.Wellbore flow and heat transfer of foam drilling fluid[J].Acta Petrolei Sinica,2010,31(1):134-138.
[5]Ramey H J.Wellbore heat transmission[J].JPT,1962,14(4):427-435.
[6]Hasan A R,Kabir C S.Aspects of wellbore heat transfer during two phase flow[R].SPE 22948,1994.
[7]李颖川,王志彬,钟海泉.注蒸汽井井筒热传递的定量计算[J].石油学报,2010,31(3):318-321.
Li Yingchuan,Wang Zhibin,Zhong Haiquan.Annulus pressure unloading technology against generation of natural gas hydrate in the wellbore of gas well[J].Acta Petrolei Sinica,2010,31(3):318-321.
[8]林日亿,李兆敏.井筒中蒸汽氮气混合物流动与换热规律[J].石油学报,2010,31(3):506-510.
Lin Riyi,Li Zhaomin.Flow features and heat exchange laws of steam-nitrogen mixture in thermal recovery wellbore[J].Acta Petrolei Sinica,2010,31(3):506-510.
[9]王弥康.注蒸汽井井筒热传递的定量计算[J].石油大学学报:自然科学版,1994,18(4):77-82.
Wang Mikang.Quantitative calculation of wellbore heat transmission for steam injection wells[J].Journal of the University of Petroleum,China:Edition of Natural Science,1994,18(4):77-82.
[10]吴晓东,王庆,何岩峰.考虑相态变化的注CO2 井筒温度、压力场耦合计算[J].中国石油大学学报:自然科学版,2009,33(1):73-77.
Wu Xiaodong,Wang Qing,He Yanfeng.Temperature-pressure field coupling calculation model considering phase behavior change in CO2 injection well borehole[J].Journal of China University of Petroleum:Edition of Natural Science,2009,33(1):73-77.
[11]郭绪强,荣淑霞,杨继涛,等.基于PR状态方程的黏度计算模型[J].石油学报,1999,20(3):56-61.
Guo Xuqiang,Rong Shuxia,Yang Jitao,et al.The viscosity model based on PR equation of state[J].Acta Petrolei Sinica,1999,20(3):56-61.
[12]童景山.流体热物性学—基本理论与计算[M].北京:中国石化出版社,2008:142.
Tong Jingshan.Fluid thermophysical property—basic theory and calculation[M].Beijing:China Petrochemical Press,2008:142.
[13]董正远,肖荣鸽.计算天然气焦耳-汤姆逊系数的BWRS方法[J].油气储运,2006,26(1):18-22.
Dong Zhengyuan,Xiao Rongge.The BWRS method for calculation natural gas Joule-Thomson coefficient[J].Oil & Gas Storage and Transportation,2006,26(1):18-22.
[14]Churchill S W.Friction-factor equation spans all fluid-flow regimes[J].Chemical Engineering,1977,84(24):91-92.
[15]王庆,吴晓东,刘长宇,等.CO2 井筒相变流动温度压力计算模型研究[J].钻采工艺,2009,32(4):56-61.
Wang Qing,Wu Xiaodong,Liu Changyu,et al.Study on model of temperature and pressure distribution in CO2 wellbore flow including the fluid phase change[J].Drilling & Production Technology,2009,32(4):56-61. |