LIQUID-SOLID MASS TRANSFER IN A TRICKLE-BED REACTOR MEASURED BY MEANS OF A CATALYTIC REACTION.

M. Herskowitz; M. Abuelhaija

LIQUID-SOLID MASS TRANSFER IN A TRICKLE-BED REACTOR MEASURED BY MEANS OF A CATALYTIC REACTION.

Department of Chemical Engineering

Research output: Contribution to journal › Conference article › peer-review

Abstract

Global rates of reaction (the hydrogenation of cyclohexene to cyclohexane on Pd/Al//2O//3) were measured in a trickle-bed reactor at various gas and liquid flow rates. Liquid-solid mass transfer coefficients were calculated from the rate data. In the low interaction regime, the coefficients depend on both the gas and liquid rates. At the transition to the high interaction regime, a significant change in the values of the coefficients was observed. The experimental liquid-solid mass transfer coefficients are in good agreement with values predicted by correlations published in the literature.

Original language	English
Journal	Annual Meeting - American Institute of Chemical Engineers
State	Published - 1 Dec 1985

ASJC Scopus subject areas

General Engineering

Cite this

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title = "LIQUID-SOLID MASS TRANSFER IN A TRICKLE-BED REACTOR MEASURED BY MEANS OF A CATALYTIC REACTION.",

abstract = "Global rates of reaction (the hydrogenation of cyclohexene to cyclohexane on Pd/Al//2O//3) were measured in a trickle-bed reactor at various gas and liquid flow rates. Liquid-solid mass transfer coefficients were calculated from the rate data. In the low interaction regime, the coefficients depend on both the gas and liquid rates. At the transition to the high interaction regime, a significant change in the values of the coefficients was observed. The experimental liquid-solid mass transfer coefficients are in good agreement with values predicted by correlations published in the literature.",

author = "M. Herskowitz and M. Abuelhaija",

year = "1985",

month = dec,

day = "1",

language = "English",

journal = "Annual Meeting - American Institute of Chemical Engineers",

issn = "0196-7282",

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AU - Herskowitz, M.

AU - Abuelhaija, M.

PY - 1985/12/1

Y1 - 1985/12/1

N2 - Global rates of reaction (the hydrogenation of cyclohexene to cyclohexane on Pd/Al//2O//3) were measured in a trickle-bed reactor at various gas and liquid flow rates. Liquid-solid mass transfer coefficients were calculated from the rate data. In the low interaction regime, the coefficients depend on both the gas and liquid rates. At the transition to the high interaction regime, a significant change in the values of the coefficients was observed. The experimental liquid-solid mass transfer coefficients are in good agreement with values predicted by correlations published in the literature.

AB - Global rates of reaction (the hydrogenation of cyclohexene to cyclohexane on Pd/Al//2O//3) were measured in a trickle-bed reactor at various gas and liquid flow rates. Liquid-solid mass transfer coefficients were calculated from the rate data. In the low interaction regime, the coefficients depend on both the gas and liquid rates. At the transition to the high interaction regime, a significant change in the values of the coefficients was observed. The experimental liquid-solid mass transfer coefficients are in good agreement with values predicted by correlations published in the literature.

UR - http://www.scopus.com/inward/record.url?scp=0022204030&partnerID=8YFLogxK

M3 - Conference article

AN - SCOPUS:0022204030

SN - 0196-7282

JO - Annual Meeting - American Institute of Chemical Engineers

JF - Annual Meeting - American Institute of Chemical Engineers

ER -

LIQUID-SOLID MASS TRANSFER IN A TRICKLE-BED REACTOR MEASURED BY MEANS OF A CATALYTIC REACTION.

Abstract

ASJC Scopus subject areas

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