作者:杜庆军;侯健;鹿腾;李振泉;张言辉; 时间:2010-01-01 点击数:
杜庆军;侯健;鹿腾;李振泉;张言辉;
1:中国石油大学(华东)地球资源与信息学院
2:中国石油大学(华东)石油工程学院
3:胜利石油管理局地质科学研究院
摘要(Abstract):
基于泡沫临界毛管力理论,建立描述泡沫驱渗流特征的分流量方程,采用特征线法进行求解;通过对泡沫驱替实验进行拟合,研究有前置表面活性剂段塞和无前置表面活性剂段塞的泡沫驱渗流特征.结果表明:该方法可以从机理上反映泡沫驱渗流特征;在有前置表面活性剂段塞情况下,泡沫体系呈活塞式驱替,岩心两端压力线性增加,驱替前缘两侧分别为水流动区和泡沫流动区,其中泡沫流动区处于临界含水饱和度状态;在无前置表面活性剂段塞情况下,水流动区和泡沫流动区之间存在自由气和水混合流动的气驱段塞,同时泡沫突破时间晚于有表面活性剂段塞情况,但容易产生气窜现象.
关键词(KeyWords):泡沫驱;渗流特征;分流理论;物理模拟
Abstract:
Keywords:
基金项目(Foundation):国家“863”项目(2007AA06Z216);;
国家自然科学基金项目(10972237);;
国家科技重大专项(2008ZX05011)
作者(Author):杜庆军;侯健;鹿腾;李振泉;张言辉;
Email:
参考文献(References):
[1]廖广志,李立众,孔繁华,等.常规泡沫驱油技术[M].北京:石油工业出版社,1999.
[2]张思富,廖广志,张彦庆,等.大庆泡沫复合驱油先导性矿场试验[J].石油学报,2001,22(1):49-53.
[3]周国华,宋新旺,王其伟,等.泡沫复合驱在胜利油田的应用[J].石油勘探与开发,2006,33(3):369-373.
[4]张莉,郭兰磊,任韶然,等.埕东油田强化泡沫驱矿场驱油效果[J].大庆石油学院学报,2010,34(1):47-50.
[5]Ettinger R A,Radke C J.Influence of texture on steady foam flow in berea sandstone[C].SPE 19688,1992.
[6]杜庆军,侯健,李振泉,等.聚合物强化泡沫驱数学模型及其应用[J].计算物理,2009,26(6):879-885.
[7]Marfoe C H,Kazemi H,Ramirez W F.Numerical simulation of foam flow in porous media[C].SPE 16709,1987.
[8]Fisher A W,Foulser R W S,Goodyear S G.Mathematical modeling of foam flooding[C].SPE 20195,1990.
[9]Cheng Lin-song,Xiao Shuang-ai.Numerical simulation of steam-foam flooding for heavy oil reservoir[J].Chinese Journal of Computa-tion Physics,2003,20(5):463-466.
[10]Falls A H,Gauglitz P A,Hirasaki G J,et al.Development of a mechanistic foam simulator:the population balance and generationby snap-off[C].SPE 14961,1986.
[11]Kovscek A R,Patzek T W,Radke C J.Simulation of foam transport in porous media[C].SPE 26402,1993.
[12]Kovscek A R,Patzek T W,Radke C J.Mechanistic prediction of foam displacement in multidimensions:a population balance ap-proach[C].SPE 27789,1994.
[13]Rossen W R,Zhou Z H,Mamun C K.Modeling foam mobility in porous media[C].SPE 22627,1991.
[14]Shi Jianxin,Rossen W R.Simulation and dimensional analysis of foam processes in porous media[C].SPE 35166,1996.
[15]Rossen W R,Gauglitz P A.Percolation theory of creation and mobilization of foam in porous media[C].AIChEJ,1990,36:1176.
[16]Kharabaf H,Yortsos Y C.Pore network model for foam formation and propagation in porous media[C].SPE 36663,1996.
[17]Chen M,Yortsos Y C,Rossen W R.A pore-network study of the mechanisms of foam generation[C].SPE 90939,2004.
[18]Khatib Z I,Hirasaki G J,Falls A H.Effects of capillary pressure on coalescence and phase mobilities in foams flowing through por-ous media[C].SPE 15442,1988.
[19]Fisher A W,Foulser R W S,Goodyear S G,et al.Mathematical modeling of foam flooding[C].SPE 20195,1990.
[20]Persoff P,Radke C J,Pruess K,et al.A laboratory investigation of foam flow in sandstone at elevated pressure[C].SPE 18781,1991.
[21]Radke C J,Gillis J V.A dual gas tracer technique for determining trapped gas saturation during steady foam flow in porous media[C].SPE 20519,1990.
[22]王玉斗,商永涛.泡沫对气液相对渗透率影响研究[J].石油天然气学报,2008,30(4):146-149.
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