A Review of Molybdenum Catalysts for Synthesis Gas Conversion to Alcohols: Catalysts, Mechanisms and Kinetics

被引:237
作者
Zaman, Sharif [1 ]
Smith, Kevin J. [1 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, Vancouver, BC V6T 1Z3, Canada
来源
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING | 2012年 / 54卷 / 01期
基金
加拿大自然科学与工程研究理事会;
关键词
Synthesis gas; alcohols; catalysts; promoters; molybdenum; CO adsorption; CO dissociation; DFT; DENSITY-FUNCTIONAL THEORY; CARBON-DIOXIDE HYDROGENATION; CHEMICAL-POTENTIAL ANALYSIS; TRANSITION-METAL CARBIDES; MOS2; 100; SURFACE; CO ADSORPTION; MIXED ALCOHOLS; AB-INITIO; SHIFT REACTION; METHANOL SYNTHESIS;
D O I
10.1080/01614940.2012.627224
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Recent literature on synthesis gas conversion to higher alcohols over Mo-based catalysts is reviewed. Density functional theory calculations show that Mo-CO adsorption is weakened by C, P, or S ligands and this facilitates CO dissociation, either directly on Mo2C, or by H-assisted dissociation on MoS2, Mo2C, and MoP. Consequently, Mo-based catalysts have high hydrocarbon selectivity unless they are promoted with alkali metals and/or Group VIII metals. Promoted MoS2 and MoP have alcohol selectivities of similar to 80 C atom % (CO2-free basis) at typical operating conditions (5-8 MPa, H-2/CO = 2-1, 537-603 K), whereas on promoted Mo2C, alcohol selectivities are similar to 60%. The kinetics of the synthesis gas conversion reactions over Mo-based catalysts have mostly been described by empirical power law models and the alcohol and hydrocarbon product distributions are consistent with a CO insertion mechanism for chain growth.
引用
收藏
页码:41 / 132
页数:92
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