Integrated process of coal pyrolysis and CO2 reforming of methane with and without using dielectric barrier discharge plasma

被引:5
作者
He, Xinfu [1 ]
Hu, Haoquan [1 ]
Jin, Lijun [1 ]
Hua, Wei [1 ]
机构
[1] Dalian Univ Technol, Sch Chem Engn, Inst Coal Chem Engn, State Key Lab Fine Chem, Dalian 116024, Peoples R China
基金
国家高技术研究发展计划(863计划); 中国国家自然科学基金;
关键词
CO2; reforming; coal pyrolysis; DBD plasma; methane; tar; CARBON-DIOXIDE; CATALYST; HYDROPYROLYSIS; TEMPERATURE; CONVERSION; REACTOR;
D O I
10.1080/15567036.2011.650277
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
The integrated processes of Shenmu subbituminous coal pyrolysis and CO2 reforming of methane over catalyst (Ni/SiO2) with and without using dielectric barrier discharge plasma (ICCP and ICCC) were carried out to check the effectiveness of the integrated process on improving the tar yield of coal pyrolysis. The effects of the pyrolysis temperature and time on product yields were investigated. The results indicate that both the ICCC and ICCP have an effect on increasing the tar yield compared with coal pyrolysis under N-2 or H-2. The tar yield increases with the increase of pyrolysis temperature and time in the ICCC, while relatively lower pyrolysis temperature and shorter pyrolysis time is preferable in the ICCP. The highest tar yield is 24.8 wt% at 600 degrees C for 22 min in the ICCC and that is 23.7 wt% at 500 degrees C for 7 min in the ICCP.
引用
收藏
页码:613 / 620
页数:8
相关论文
共 19 条
  • [1] COAL HYDROMETHANOLYSIS WITH COKE-OVEN GAS .1. INFLUENCE OF TEMPERATURE ON THE PYROLYSIS YIELDS
    BRAEKMANDANHEUX, C
    CYPRES, R
    FONTANA, A
    LAURENT, P
    VANHOEGAERDEN, M
    [J]. FUEL, 1992, 71 (03) : 251 - 255
  • [2] Carbon dioxide reforming of methane over Ni/Al2O3 treated with glow discharge plasma
    Cheng, Dang-guo
    Zhu, Xinli
    Ben, Yuheng
    He, Fei
    Cui, Lan
    Liu, Chang-jun
    [J]. CATALYSIS TODAY, 2006, 115 (1-4) : 205 - 210
  • [3] LOW-TEMPERATURE HYDROPYROLYSIS OF COAL UNDER PRESSURE OF H-2-CH4 MIXTURES
    CYPRES, R
    FURFARI, S
    [J]. FUEL, 1982, 61 (08) : 721 - 724
  • [4] Direct conversion of methane and carbon dioxide to higher hydrocarbons using catalytic dielectric-barrier discharges with zeolites
    Eliasson, B
    Liu, CJ
    Kogelschatz, U
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (05) : 1221 - 1227
  • [5] Fridman A., 2008, PLASMA CHEM
  • [6] Integrated Process of Coal Pyrolysis with CO2 Reforming of Methane by Dielectric Barrier Discharge Plasma
    He, Xinfu
    Jin, Lijun
    Wang, Ding
    Zhao, Yunpeng
    Zhu, Shengwei
    Hu, Haoquan
    [J]. ENERGY & FUELS, 2011, 25 (09) : 4036 - 4042
  • [7] Catalytic liquefaction of coal with highly dispersed Fe2S3 impregnated in-situ
    Hu, HQ
    Bai, JF
    Zhu, HJ
    Wang, Y
    Guo, SC
    Chen, GH
    [J]. ENERGY & FUELS, 2001, 15 (04) : 830 - 834
  • [8] Hua W., 2009, P 10 JAP CHIN S COAL
  • [9] Preparation of Ni/MgO catalyst for CO2 reforming of methane by dielectric-barrier discharge plasma
    Hua, Wei
    Jin, Lijun
    He, Xinfu
    Liu, Jiahe
    Hu, Haoquan
    [J]. CATALYSIS COMMUNICATIONS, 2010, 11 (11) : 968 - 972
  • [10] Partial oxidation of methane with yttria-stabilized zirconia catalyst in a dielectric barrier discharge
    Indarto, A.
    Lee, H.
    Choi, J. -W.
    Song, H. K.
    [J]. ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2008, 30 (17) : 1628 - 1636