Interaction of Kerogen Combustion and Pyrolysis and Continuous Oil Production during In Situ Combustion for Oil Shale Upgrading

被引:4
作者
Cui, Guodong [1 ,2 ,3 ]
Yang, Lihong [4 ,5 ]
Pei, Shufeng [6 ]
Fang, Jichao [7 ]
机构
[1] State Key Lab Shale Oil & Gas Enrichment Mech & Ef, Beijing 100083, Peoples R China
[2] Ctr Res & Dev Oil Shale Exploitat, Beijing 100083, Peoples R China
[3] China Univ Geosci, Fac Engn, Wuhan 430074, Peoples R China
[4] Sinopec Petr Explorat & Prod Res Inst, Beijing 100083, Peoples R China
[5] Sinopec Petr Explorat & Prod Res Inst, Beijing 100083, Peoples R China
[6] Sinopec Shengli Oilfield Co, Petr Engn Res Inst, Dongying 257000, Peoples R China
[7] Sinopec Petr Explorat & Prod Res Inst, Beijing 100083, Peoples R China
基金
中国国家自然科学基金;
关键词
Oil shale; In situ combustion; Kerogen pyrolysis; Energy efficiency; LOW-TEMPERATURE OXIDATION; NUMERICAL-SIMULATION; COMPREHENSIVE UTILIZATION; CRUDE-OIL; RESERVOIR; MODEL; TECHNOLOGY; MECHANISM; KINETICS; PROGRESS;
D O I
10.1061/JLEED9.EYENG-5195
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
Oil shale is a potential strategic resource with large reserves and widespread application potential, and in situ combustion is an effective method to exploit oil shale. However, the interaction mechanism between pyrolysis and combustion reaction is still not clear; hence, the evolution of components and temperature in the reservoir is hard to describe, limiting the application of in situ combustion in oil shale. In this paper, we established a comprehensive reactive flow model to describe the in situ combustion in oil shale, and the in situ combustion process is analyzed in detail. During the in situ combustion, only pyrolysis reactions occur in the matrix system, while combustion reactions only occur in the fracture system. Under the interaction mechanisms of these two kinds of chemical reactions, in situ combustion upgrading can be carried out continuously. The produced oil and hydrocarbon gas per unit volume of oil shale are 0.06 m3/m3 and 12.5 m3/m3, respectively, but about 83.3 m3/m3 of CO2 is produced that needs to be stored subsequently when air is directly injected into the reservoir to maintain the combustion reactions. Increasing oil content and air injection rate can increase the cumulative oil and gas production, but there are optimal values above which the increase rate slows down. The energy conversion efficiency of in situ combustion is 49.5, and it is much higher than the energy conversion efficiency in other in situ upgrading methods for oil shale.
引用
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页数:13
相关论文
共 40 条
[1]   Thermogravimetric Analysis of Huadian Oil Shale Combustion at Different Oxygen Concentrations [J].
Bai, Fengtian ;
Sun, Youhong ;
Liu, Yumin .
ENERGY & FUELS, 2016, 30 (06) :4450-4456
[2]   Thermal and kinetic characteristics of pyrolysis and combustion of three oil shales [J].
Bai, Fengtian ;
Sun, Youhong ;
Liu, Yumin ;
Li, Qiang ;
Guo, Mingyi .
ENERGY CONVERSION AND MANAGEMENT, 2015, 97 :374-381
[3]  
Bai W., 2019, Surface thermal injecting system for oil shale in-situ pyrolysis and thermal efficiency analysis
[4]   MATHEMATICAL-MODEL FOR INSITU OIL-SHALE RETORTING BY ELECTROMAGNETIC-RADIATION [J].
BAKERJARVIS, J ;
INGUVA, R .
FUEL, 1988, 67 (07) :916-926
[5]   PMOD - A FLEXIBLE MODEL OF OIL AND GAS GENERATION, CRACKING, AND EXPULSION [J].
BRAUN, RL ;
BURNHAM, AK .
ORGANIC GEOCHEMISTRY, 1992, 19 (1-3) :161-172
[6]  
Burnham A.K, 2006, Comparison of the Acceptability of Various Oil Shale Processes M
[7]  
Burwell E, 1970, J PETROL TECHNOL, V22, P1520
[8]  
Burwell EL, 1973, In situ retorting of oil shale: Results of two field experiments, 7781-7800
[9]  
Crawford P. M., 2008, PROC PAPER PRESENTED
[10]   Migration characteristics and local capillary trapping mechanism after the CO2 leakage out of saline aquifers [J].
Cui, Guodong ;
Hu, Zhe ;
Wang, Yanyong ;
Jiang, Shu ;
Wang, Rui .
FUEL, 2024, 356