Hydrogenation of benzaldehyde to benzyl alcohol in a slurry and fixed-bed reactor

M. Herskowitz

doi:10.1016/S0167-2991(08)61110-6

Hydrogenation of benzaldehyde to benzyl alcohol in a slurry and fixed-bed reactor

M. Herskowitz

Department of Chemical Engineering

Research output: Contribution to journal › Article › peer-review

11 Scopus citations

Abstract

A kinetic model was developed based on data obtained over a range of temperatures and hydrogen pressures. The kinetic parameters were expressed as a function of temperature. The kinetic model was applied to the analysis of the trickle-bed data. Predictions of a mathematical model of the trickle-bed reactor were compared with data obtained at two temperatures and a range of pressures. The intraparticle mass transfer resistance was very important.

Original language	English
Pages (from-to)	105-112
Number of pages	8
Journal	Studies in Surface Science and Catalysis
Volume	59
Issue number	C
DOIs	https://doi.org/10.1016/S0167-2991(08)61110-6
State	Published - 1 Jan 1991

ASJC Scopus subject areas

Catalysis
Condensed Matter Physics
Physical and Theoretical Chemistry
Surfaces, Coatings and Films
Materials Chemistry

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10.1016/S0167-2991(08)61110-6

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title = "Hydrogenation of benzaldehyde to benzyl alcohol in a slurry and fixed-bed reactor",

abstract = "A kinetic model was developed based on data obtained over a range of temperatures and hydrogen pressures. The kinetic parameters were expressed as a function of temperature. The kinetic model was applied to the analysis of the trickle-bed data. Predictions of a mathematical model of the trickle-bed reactor were compared with data obtained at two temperatures and a range of pressures. The intraparticle mass transfer resistance was very important.",

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N2 - A kinetic model was developed based on data obtained over a range of temperatures and hydrogen pressures. The kinetic parameters were expressed as a function of temperature. The kinetic model was applied to the analysis of the trickle-bed data. Predictions of a mathematical model of the trickle-bed reactor were compared with data obtained at two temperatures and a range of pressures. The intraparticle mass transfer resistance was very important.

AB - A kinetic model was developed based on data obtained over a range of temperatures and hydrogen pressures. The kinetic parameters were expressed as a function of temperature. The kinetic model was applied to the analysis of the trickle-bed data. Predictions of a mathematical model of the trickle-bed reactor were compared with data obtained at two temperatures and a range of pressures. The intraparticle mass transfer resistance was very important.

UR - https://www.scopus.com/pages/publications/0010635972

U2 - 10.1016/S0167-2991(08)61110-6

DO - 10.1016/S0167-2991(08)61110-6

M3 - Article

AN - SCOPUS:0010635972

SN - 0167-2991

VL - 59

SP - 105

EP - 112

JO - Studies in Surface Science and Catalysis

JF - Studies in Surface Science and Catalysis

IS - C

ER -

Hydrogenation of benzaldehyde to benzyl alcohol in a slurry and fixed-bed reactor

Abstract

ASJC Scopus subject areas

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