A new process for catalytic liquefaction of coal using dispersed MoS2 catalyst generated in situ with added H2O

被引:36
作者
Song, C
Saini, AK
Yoneyama, Y
机构
[1] Penn State Univ, Appl Catalysis Energy Lab, Energy Inst, University Pk, PA 16802 USA
[2] Penn State Univ, Dept Energy & Geoenvironm Engn, University Pk, PA 16802 USA
关键词
coal; liquefaction; catalyst; molybdenum sulfide; water; synergetic effect; temperature-programmed liquefaction;
D O I
10.1016/S0016-2361(99)00159-3
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
We have found that adding a proper amount of water can dramatically improve conversion of a sub-bituminous coal in solvent-free liquefaction under at 350 degrees C using ammonium tetrathiomolybdate (ATTM) as precursor to dispersed MoS2 catalyst H-2 pressure. However, adding water to catalytic reactions at 400 degrees C decreased coal conversion, although water addition to the nun-catalytic runs was slightly beneficial at this temperature. We further examined the effect of water in solvent-mediated runs in addition to "dry" tests and explored a temperature-programmed liquefaction (TPL) procedure to take advantage of the synergetic effect between water and dispersed Mo catalyst precursor at low temperatures for more efficient coal conversion The TPL using ATTM with added water at 350 degrees C, followed by water removal and subsequent reaction at 400 degrees C gave good coal conversion and oil yield. Model reactions of dinaphthyl ether (DNE) were also carried out to clarify the effect of water. Addition of water to ATTM substantially enhanced DNE conversion at 350 degrees C, The combination of data from one-step and two-step tests of DNE and coal at 350-400 degrees C revealed that water results in highly active MoS2 catalyst in situ generated at 350 degrees C, but water does not promote the catalytic function or reaction once an active catalyst is generated. Using ATTM coupled with water addition and removal and temperature-programming may be an effective strategy for developing a better coal conversion process using dispersed catalysts. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:249 / 261
页数:13
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