CO2 huff and puff for heavy oil recovery after primary production

被引:14
作者
Lu, Teng [1 ]
Li, Zhaomin [1 ]
Fan, Weiyu [2 ]
Li, Songyan [3 ]
机构
[1] China Univ Petr, Qingdao 266580, Peoples R China
[2] China Univ Petr, Chem Engn, Qingdao 266580, Peoples R China
[3] China Univ Petr, Petr Engn, Qingdao 266580, Peoples R China
基金
中国博士后科学基金;
关键词
CO2 huff and puff; heavy oil; foamy oil; solution gas drive; SOLUTION-GAS DRIVE; FOAMY OIL; N-PUFF; RESERVOIR; MOBILITY; BITUMEN;
D O I
10.1002/ghg.1566
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
In this study, micromodel tests were performed to investigate the microscopic flow behavior during primary production and the subsequent CO2 huff and puff. A series of 12 tests was conducted in sandpacks to evaluate the effects of the injection and production parameters on the displacement efficiency of the CO2 huff and puff. The micromodel tests and sandpack tests showed that the flow characteristics of CO2 huff-and-puff process was significantly affected by the pressure of converting the solution gas drive to the subsequent CO2 huff and puff. A foamy oil flow could be more easily formed in the production period of the CO2 huff and puff with a higher conversion pressure. Foamy oil can reduce the mobility of gas and provide tremendous energy to the system, thereby improving the performance of the CO2 huff and puff. The sandpack flood results show that the oil recovery of the solution gas drive decreased as the conversion pressure increased, whereas the oil recovery of the CO2 huff and puff increased as the conversion pressure increased. The highest total oil recovery was obtained at the pseudo-bubblepoint pressure. The oil recovery of the CO2 huff and puff increased as the CO2 injection pressure and pressure decline rate increased. The oil recovery of CO2 huff and puff increased with the soaking time, and it exhibits a significant change when the soaking time ranges from 10 h to 24 h; above this value, the increase become slight. (c) 2015 Society of Chemical Industry and John Wiley & Sons, Ltd
引用
收藏
页码:288 / 301
页数:14
相关论文
共 30 条
[1]  
[Anonymous], SPE ANN TECHN C EXH
[2]  
Bennion DB, 2003, J CAN PETROL TECHNOL, V42, P21
[3]  
Bybee K., 2007, Journal of Petroleum Technology, V59, P55, DOI DOI 10.2118/0107-0055-JPT
[4]   Methane pressure-cycling process with horizontal wells for thin heavy-oil reservoirs [J].
Dong, MZ ;
Huang, S ;
Hutchence, K .
SPE RESERVOIR EVALUATION & ENGINEERING, 2006, 9 (02) :154-164
[5]   Dominant Scaling Groups of Polymer Flooding for Enhanced Heavy Oil Recovery [J].
Guo, Ziqiang ;
Dong, Mingzhe ;
Chen, Zhangxin ;
Yao, Jun .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (02) :911-921
[6]   Investigation of Cyclic Solvent Injection Process for Heavy Oil Recovery [J].
Ivory, J. ;
Chang, J. ;
Coates, R. ;
Forshner, K. .
JOURNAL OF CANADIAN PETROLEUM TECHNOLOGY, 2010, 49 (09) :22-33
[7]   Enhanced Cyclic Solvent Process (ECSP) for Heavy Oil and Bitumen Recovery in Thin Reservoirs [J].
Jamaloei, Benyamin Yadali ;
Dong, Mingzhe ;
Mahinpey, Nader ;
Maini, Brij B. .
ENERGY & FUELS, 2012, 26 (05) :2865-2874
[8]   Analysis and Correlations of Viscous Fingering in Low-Tension Polymer Flooding in Heavy Oil Reservoirs [J].
Jamaloei, Benyamin Yadali ;
Kharrat, Riyaz ;
Torabi, Farshid .
ENERGY & FUELS, 2010, 24 (12) :6384-6392
[9]   A LABORATORY STUDY OF HEAVY OIL-RECOVERY WITH CARBON-DIOXIDE [J].
JHA, KN .
JOURNAL OF CANADIAN PETROLEUM TECHNOLOGY, 1986, 25 (02) :54-63
[10]  
KRAUS WP, 1993, ANN TECHN M PETR SOC