EFFECTS OF OPERATING PRESSURE ON COAL-GASIFICATION

被引:36
|
作者
SHA, XZ
CHEN, YG
CAO, JG
YANG, YM
REN, DQ
机构
[1] East China Institute of Chemical Technology, Shanghai, 200237
关键词
coal; gasification; hydrogasification;
D O I
10.1016/0016-2361(90)90157-L
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
Correlation of operating pressure with coal pyrolysis, coal caking, coal clinkering and coal char reactivity is very important as regards coal gasification. It is shown that irrespective of whether the pyrolysing atmosphere is N2 or H2, yields of CH4 and C2H6 increase with increasing pressure, but the yields are much higher in H2. The reactivities of coal chars obtained by pyrolysis under pressure tend to decrease with increasing pressure. The CH2O and CCO2 reactions are similar to each other, their reaction rates increase with increasing PH and PCO respectively up to 1-1.5 MPa, and then tend to have a zero order with respect to the partial pressure of reacting gases. Char combustion rates are 0.25-0.35 order with respect to PO, Coal or char hydrogasification is very sensitive to PH, a first order reaction being obtained in a broad range of operating pressure. When air flow rates are kept constant, the coal clinkering ratio increases with decreasing pressure. Trends of coal caking property change with increasing pressure depending on coal rank. Brown coals do not coagulate at normal pressure or under pressure; the caking properties of weakly caking coals increase smoothly with increasing pressure at first, and then remain constant above a characteristic pressure, while the caking properties of caking coals increase throughout the pressure range examined. © 1990.
引用
收藏
页码:656 / 659
页数:4
相关论文
共 50 条
  • [1] COAL-GASIFICATION UNDER PRESSURE
    SCHELLBERG, W
    UMSCHAU, 1985, 85 (12): : 741 - 743
  • [2] EFFECTS OF FLAME TYPE AND PRESSURE ON ENTRAINED COAL-GASIFICATION
    AZUHATA, S
    HEDMAN, PO
    SMOOT, LD
    SOWA, WA
    FUEL, 1986, 65 (11) : 1511 - 1515
  • [3] COAL-GASIFICATION
    DEHAEN, P
    JOURNAL OF THE AMERICAN SOCIETY FOR INFORMATION SCIENCE, 1980, 31 (02): : 125 - 125
  • [4] COAL-GASIFICATION
    WILKINS, DG
    MECHANICAL ENGINEERING, 1992, 114 (05) : 8 - 8
  • [5] COAL-GASIFICATION
    MOSS, SH
    SCHLINGER, WG
    LUBRICATION, 1980, 66 (03): : 25 - 36
  • [6] COAL-GASIFICATION
    KING, WEH
    FUEL, 1981, 60 (09) : 803 - 808
  • [8] FEASIBLE OPERATING REGIONS FOR MOVING BED COAL-GASIFICATION REACTORS
    YOON, H
    WEI, J
    DENN, MM
    INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1979, 18 (02): : 306 - 312
  • [9] KINETICS OF COAL-GASIFICATION
    SCHMAL, M
    MONTEIRO, JLF
    CASTELLAN, JL
    INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1982, 21 (02): : 256 - 266
  • [10] AUTOTHERMAL COAL-GASIFICATION
    KONKOL, W
    RUPRECHT, P
    CORNILS, B
    DURRFELD, R
    LANGHOFF, J
    HYDROCARBON PROCESSING, 1982, 61 (03): : 97 - 102