Establishment and application of a two-stage reaction equilibrium model for underground coal gasification

被引:1
|
作者
Li, Guangpeng [1 ,2 ,3 ,4 ]
Duan, Tianhong [2 ,3 ,4 ]
Li, Xiang [2 ,3 ,4 ]
Wang, Zuotang [2 ,3 ,4 ]
Zhang, Peng [2 ,3 ,4 ]
机构
[1] Shandong Inst Commerce & Technol, Jinan, Peoples R China
[2] China Univ Min & Technol, Sch Mines, Xuzhou 221116, Jiangsu, Peoples R China
[3] China Univ Min & Technol, State Key Lab Coal Resources & Mine Safety, Xuzhou, Peoples R China
[4] Minist Educ China, Key Lab Deep Coal Resource Min, Xuzhou, Peoples R China
关键词
field test; heat loss rate; pyrolysis; two-stage reaction equilibrium model; underground coal gasification; TEMPERATURE; PYROLYSIS; CONTEXT;
D O I
10.1002/er.8571
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
Gasification parameters are basic and original parameters in the design and operation process of gasification projects. In the present research, the conventional reaction equilibrium model was proposed to be a two-stage reaction equilibrium model to calculate the gasification parameters of underground coal gasification (UCG). The simulated pyrolysis experimental method of UCG was established to obtain the parameters of pyrolysis gas. Afterward, the appropriate heat loss rate (HLR) was determined and gasification parameters were calculated according to the modified reaction equilibrium model. Then, the ultimate gasification parameters were calculated according to the data obtained from the two-stage reaction equilibrium model. The accuracy of the proposed model was verified by comparing the calculated gasification parameters to the field testing parameters of the Ankou coal mine. The proposed two-stage modified reaction equilibrium model for UCG can be applied by considering the special characteristics of pyrolysis in UCG and the appropriate HLR value.
引用
收藏
页码:22679 / 22689
页数:11
相关论文
共 50 条
  • [21] Optimizing the gasification operating conditions of forest residues by coupling a two-stage equilibrium model with a response surface methodology
    Silva, Valter
    Rouboa, Abel
    [J]. FUEL PROCESSING TECHNOLOGY, 2014, 122 : 163 - 169
  • [22] Effect of coal particle size on gasification performance of two-stage entrained-flow coal gasifier
    Fan, Qiang
    Liu, Yinhe
    Li, Guangyu
    Che, Defu
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2021, 99 (12): : 2677 - 2690
  • [23] PREDICTION OF UNDERGROUND COAL GASIFICATION PERFORMANCE OF TURKISH LIGNITE RESERVES USING STOICHIOMETRIC EQUILIBRIUM MODEL
    Canbaz, Engin Deniz
    Gur, Mesut
    [J]. ISI BILIMI VE TEKNIGI DERGISI-JOURNAL OF THERMAL SCIENCE AND TECHNOLOGY, 2020, 40 (02) : 195 - 205
  • [24] Study on coal gasification with soot formation in two-stage entrained-flow gasifier
    Saiful Alam M.
    Wijayanta A.T.
    Nakaso K.
    Fukai J.
    [J]. International Journal of Energy and Environmental Engineering, 2015, 6 (03) : 255 - 265
  • [26] Two-Stage Equilibrium Travel Demand Model for Sketch Planning
    Xie, Chi
    Kockelman, Kara M.
    [J]. TRANSPORTATION RESEARCH RECORD, 2012, (2302) : 1 - 13
  • [27] Dynamic modelling of the two-stage gasification process
    Gobel, B
    Bentzen, JD
    Henriksen, U
    Houbak, N
    [J]. BIOMASS: A GROWTH OPPORTUNITY IN GREEN ENERGY AND VALUE-ADDED PRODUCTS, VOLS 1 AND 2, 1999, : 1025 - 1031
  • [28] Investigation of a Two-stage Process of Biomass Gasification
    Kosov, Valentin V.
    Kosov, Vladimir F.
    Zaichenko, Victor M.
    [J]. ICHEAP12: 12TH INTERNATIONAL CONFERENCE ON CHEMICAL & PROCESS ENGINEERING, 2015, 43 : 457 - 462
  • [29] Two-stage dual fluidized bed gasification: Its conception and application to biomass
    Xu, Guangwen
    Murakami, Takahiro
    Suda, Toshiyuki
    Matsuzaw, Yoshiaki
    Tani, Hidehisa
    [J]. FUEL PROCESSING TECHNOLOGY, 2009, 90 (01) : 137 - 144
  • [30] Advanced two-stage biomass gasification process
    Hamel, S.
    Krumm, W.
    [J]. VDI Berichte, 2002, (1714): : 285 - 298