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

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 Mo 2 C, or by H-assisted dissociation on...

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Veröffentlicht in:Catalysis reviews. Science and engineering 2012-01, Vol.54 (1), p.41-132
Hauptverfasser: Zaman, Sharif, Smith, Kevin J.
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description 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 Mo 2 C, or by H-assisted dissociation on MoS 2 , Mo 2 C, and MoP. Consequently, Mo-based catalysts have high hydrocarbon selectivity unless they are promoted with alkali metals and/or Group VIII metals. Promoted MoS 2 and MoP have alcohol selectivities of ∼80 C atom % (CO 2 -free basis) at typical operating conditions (5-8 MPa, H 2 /CO = 2-1, 537-603 K), whereas on promoted Mo 2 C, alcohol selectivities are ∼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.
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Science and engineering</title><description>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 Mo 2 C, or by H-assisted dissociation on MoS 2 , Mo 2 C, and MoP. Consequently, Mo-based catalysts have high hydrocarbon selectivity unless they are promoted with alkali metals and/or Group VIII metals. Promoted MoS 2 and MoP have alcohol selectivities of ∼80 C atom % (CO 2 -free basis) at typical operating conditions (5-8 MPa, H 2 /CO = 2-1, 537-603 K), whereas on promoted Mo 2 C, alcohol selectivities are ∼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.</description><subject>Alcohols</subject><subject>Carbon dioxide</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Chemistry</subject><subject>CO adsorption</subject><subject>CO dissociation</subject><subject>Conversion</subject><subject>DFT</subject><subject>Exact sciences and technology</subject><subject>General and physical chemistry</subject><subject>Molecules</subject><subject>Molybdenum</subject><subject>Molybdenum disulfide</subject><subject>promoters</subject><subject>Reaction kinetics</subject><subject>Selectivity</subject><subject>Surface physical chemistry</subject><subject>Synthesis gas</subject><subject>Theory of reactions, general kinetics. Catalysis. 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subjects Alcohols
Carbon dioxide
Catalysis
Catalysts
Chemistry
CO adsorption
CO dissociation
Conversion
DFT
Exact sciences and technology
General and physical chemistry
Molecules
Molybdenum
Molybdenum disulfide
promoters
Reaction kinetics
Selectivity
Surface physical chemistry
Synthesis gas
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
title A Review of Molybdenum Catalysts for Synthesis Gas Conversion to Alcohols: Catalysts, Mechanisms and Kinetics
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