Comparative Study of the Gasification of Coal and Its Macerals and Prediction of the Synergistic Effects Under Typical Entrained-Bed Pulverized Coal Gasification Conditions

被引:5
|
作者
Jiang, Peng [1 ]
Guo, Dengting [1 ]
Luo, Xiang [1 ]
Xu, Mengxia [1 ]
Wu, Tao [1 ]
机构
[1] Univ Nottingham Ningbo China, Key Lab Clean Energy Convers Technol, Ningbo 315100, Peoples R China
来源
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME | 2020年 / 142卷 / 03期
关键词
coal macerals; entrained-bed gasification; synergistic effects; Aspen Plus; energy conversion; fuel combustion; CHEMICAL-LOOPING COMBUSTION; POWER; PYROLYSIS; BIOMASS; CO2-GASIFICATION; EQUILIBRIUM; INERTINITE; VITRINITE; KINETICS; BEHAVIOR;
D O I
10.1115/1.4044552
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
This research is focused on the gasification performance of coal and its corresponding macerals as well as on the interactions among macerals under typical gasification conditions by Aspen Plus modeling. The synergistic coefficient was employed to show the degree of interactions, while the performance indicators including specific oxygen consumption (SOC), specific coal consumption (SCC), cold gas efficiency (CGE), and effective syngas (CO+ H-2) content were used to evaluate the gasification process. Sensitivity analyses showed that the parent coal and its macerals exhibited different gasification behaviors at the same operating conditions, such as the SOC and SCC decreased in the order of inertinite > vitrinite > liptinite, whereas CGE changed in the order of liptinite > vitrinite > inertinite. The synergistic coefficients of SOC and SCC for the simulated coals were in the range of 0.94-0.97, whereas the synergistic coefficient of CGE was 1.05-1.13. Moreover, it was found that synergistic coefficients of gasification indicators correlated well with maceral contents. In addition, the increase in temperature was found to promote the synergistic coefficients slightly, whilst at an oxygen to coal mass ratio of 0.8 and a steam to coal mass ratio of 0.8, the highest synergistic coefficient was obtained.
引用
收藏
页数:10
相关论文
共 18 条
  • [1] CFD modeling for coal size effect on coal gasification in a two-stage commercial entrained-bed gasifier with an improved char gasification model
    Jeong, Hyo Jae
    Seo, Dong Kyun
    Hwang, Jungho
    APPLIED ENERGY, 2014, 123 : 29 - 36
  • [2] Integration of pyrolysis and entrained-bed gasification for the production of chemicals from Victorian brown coal - Process simulation and exergy analysis
    Dai, Baiqian
    Zhang, Lei
    Cui, Jian-fang
    Hoadley, Andrew
    Zhang, Lian
    FUEL PROCESSING TECHNOLOGY, 2017, 155 : 21 - 31
  • [3] Effects of oil shale on PM10 formation during Zhundong coal gasification under entrained flow gasification conditions
    Huang, Lei
    Zhang, Xianxian
    Kong, Lingxue
    Li, Huaizhu
    Bai, Zongqing
    Bai, Jin
    Li, Wen
    JOURNAL OF THE ENERGY INSTITUTE, 2024, 114
  • [4] Numerical study on coal gasification in supercritical water fluidized bed and exploration of complete gasification under mild temperature conditions
    Fan, Chao
    Guo, Simao
    Jin, Hui
    CHEMICAL ENGINEERING SCIENCE, 2019, 206 : 134 - 145
  • [5] Compartment modeling of coal gasification in an entrained flow gasifier: A study on the influence of operating conditions
    Kong, Xiangdong
    Zhong, Weimin
    Du, Wenli
    Qian, Feng
    ENERGY CONVERSION AND MANAGEMENT, 2014, 82 : 202 - 211
  • [6] Synergistic Effects of the Co-gasification of Solid Recovered Fuel and Coal Blend Using Entrained Flow Technology
    Khan, Haider
    Adeyemi, Idowu
    Janajreh, Isam
    WASTE AND BIOMASS VALORIZATION, 2025, 16 (01) : 153 - 174
  • [7] Comparative study of chemical speciation and leaching feature of typical heavy metals in coarse and fine slags from the entrained-flow coal gasification
    Lyu, Feiyong
    Chu, Mo
    Sun, Xingbo
    Cao, Shengjun
    Dong, Jianfei
    Liu, Shengnan
    ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2024, 46 (01) : 3918 - 3929
  • [8] Optimization study on operation conditions of an industrial-scale circulating fluidized bed coal gasification
    Zhan, Yueping
    Zhu, Zhiping
    Wang, Dongyu
    Lyu, Qinggang
    FUEL, 2022, 319
  • [9] From coal towards renewables: Catalytic/synergistic effects during steam co-gasification of switchgrass and coal in a pilot-scale bubbling fluidized bed
    Masnadi, Mohammad S.
    Grace, John R.
    Bi, Xiaotao T.
    Lim, C. Jim
    Ellis, Naoko
    Li, Yong Hua
    Watkinson, A. Paul
    RENEWABLE ENERGY, 2015, 83 : 918 - 930
  • [10] Determination of the Intrinsic Gasification Kinetics of a Bituminous Coal Including Product Gas Inhibition and Char Deactivation Under Entrained Flow Conditions
    Netter, Tobias
    Geissler, Andreas
    Spliethoff, Hartmut
    JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 2020, 142 (07):