Numerical simulation study on chemical ignition process of underground coal gasification

被引:0
|
作者
Zhang, Haoyu [1 ]
Xiao, Yi [1 ]
Luo, Guangqian [1 ,2 ]
Fang, Can [1 ]
Zou, Renjie [1 ,2 ]
Zhang, Youjun [3 ]
Li, Xian [1 ]
Yao, Hong [1 ]
机构
[1] Huazhong Univ Sci & Technol, State Key Lab Coal Combust, Wuhan 430074, Peoples R China
[2] Shenzhen Huazhong Univ Sci, Technol Res Inst, Shenzhen 518000, Peoples R China
[3] Natl Petr Corp, Jianghan Machinery Res Inst Ltd Co China, Wuhan 430021, Peoples R China
基金
中国国家自然科学基金;
关键词
Underground coal gasification; Chemical ignition; Excess air coefficient; Flame temperature; Ignition criterion; N-HEPTANE; PHYSICAL-PROPERTIES; CAVITY GROWTH; PART I; COMBUSTION; MODEL; UCG; PRESSURE; SLAB;
D O I
10.1016/j.energy.2024.131350
中图分类号
O414.1 [热力学];
学科分类号
摘要
Underground coal gasification (UCG) is a process that produces combustible gas by the in -situ gasification of coal seams. For a steady and efficient gasification project, the ignition of coal seam is a prerequisite. The heating method and reacting process of coal seam play an essential role to the ignition. A coal seam ignition model coupled with heptane combustion was created to simulate the deep UCG ignition stage employing the chemical ignition method. A 1700 K heptane jet flame and a U-shaped pyrolysis gas flame formed the heat source. The flame temperature of pyrolysis gas was around 1300 K. The effective heating length of the flame increased with the heating time, which reached 600 mm at 400 s. The coal seam reaction process was divided into four stages: (1) heptane flame stabilization, (2) coal seam heating, (3) pyrolysis gas release, and (4) pyrolysis gas flame stabilization. It was the third stage when the coal seam ignited. The coal seam would ignite faster with a lower excess air coefficient, and the ignition time ranged from 225 to 275 s when the excess air coefficient was 1.39. The outlet carbon dioxide concentration increased by about 5 % - 17 % when the coal seam ignited.
引用
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页数:9
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