A novel technique combining the cyclic steam stimulation and top gas injection for increasing heat efficiency

被引:1
作者
Suranto, A. M. [1 ]
机构
[1] Univ Pembangunan Nas Vet Yogyakarta, Dept Petr Engn, Yogyakarta, Indonesia
关键词
Reservoir simulation; thermal recovery; cyclic steam stimulation; top gas injection; heat efficiency;
D O I
10.1080/12269328.2017.1391717
中图分类号
P [天文学、地球科学];
学科分类号
07 ;
摘要
In the first production period of cyclic steam stimulation (CSS), the oil production rate becomes high due to reducing oil viscosity and increasing reservoir. Even though the remaining heat is still available in the surroundings of the well, the production rate declines too sharply resulting from the reservoir pressure reduction. This paper aims to maintain the oil production rate, which utilizes the remaining heat in the reservoir with a gas top injection. After the oil production rate declines, the gas is injected into the top side of the formation which pushes crude oil to the lower part of the reservoir. Finally, the crude oil moves to the production perforation. The result indicates that the optimum volume gas injection is 6500 MMSCF. In such method, increasing reservoir thickness will be more favorable because the gas spreads more laterally and dissolves to the oil phase. In the case of extended cycle production time, the steam effectiveness will increase. To get the most favorable operation condition, the reservoir thickness must be more than 20 ft. In the optimum case, the cumulative oil production increases 3.5 times and the cumulative steam oil ratio decreases 60% compared to CSS-conventional.
引用
收藏
页码:113 / 120
页数:8
相关论文
共 17 条
[1]  
Azad M., 2013, SPE KUW OIL GAS SHOW, DOI [10.2118/167378-ms, DOI 10.2118/167378-MS]
[2]   Reservoir and operational parameters influence in SAGD process [J].
Barillas, J. L. M. ;
Dutra, T. V., Jr. ;
Mata, W. .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2006, 54 (1-2) :34-42
[3]   The steam and gas push (SAGP) [J].
Butler, R .
JOURNAL OF CANADIAN PETROLEUM TECHNOLOGY, 1999, 38 (03) :54-61
[4]  
Du Y., 2013, SPE ENH OIL REC C KU, DOI [10.2118/165212-MS, DOI 10.2118/165212-MS]
[5]  
Gael B.T., 1995, SPE W REGIONAL M
[6]  
Ho D. W., 1990, EFFECTS STEAM QUALIT, DOI [10.2118/20762-MS, DOI 10.2118/20762-MS]
[7]  
Hong K. C., 1994, STEAM FLOOD RESERVOI, P13
[8]  
Jiang Q, 2000, J CAN PETROL TECHNOL, V39, P52
[9]   Steam Injection Pressure and the SAGD Ramp-Up Process [J].
Li, P. ;
Chan, M. ;
Froehlich, W. .
JOURNAL OF CANADIAN PETROLEUM TECHNOLOGY, 2009, 48 (01) :36-41
[10]  
Liu J., 2003, PETR SOC CAN INT PET, DOI [10.2118/2003-228, DOI 10.2118/2003-228]