Hydrogenation of Xylose to Xylitol

J. Wisniak; M. Hershkowitz; R. Leibowitz; S. Stein

doi:10.1021/i360049a015

Hydrogenation of Xylose to Xylitol

J. Wisniak, M. Hershkowitz, R. Leibowitz, S. Stein

Department of Chemical Engineering

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

74 Scopus citations

Abstract

Xylose has been hydrogenated with Raney nickel under a wide range of pressure, temperature, catalyst concentration, and agitation rates. The reaction follows a pseudo-first-order course with a surface-reaction-controlling step between atomically adsorbed hydrogen and adsorbed xylose at 100° and unadsorbed xylose at higher temperatures.

Original language	English
Pages (from-to)	75-79
Number of pages	5
Journal	Industrial & Engineering Chemistry Product Research and Development
Volume	13
Issue number	1
DOIs	https://doi.org/10.1021/i360049a015
State	Published - 1 Mar 1974

ASJC Scopus subject areas

General Chemistry
General Chemical Engineering
General Engineering
Industrial and Manufacturing Engineering

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title = "Hydrogenation of Xylose to Xylitol",

abstract = "Xylose has been hydrogenated with Raney nickel under a wide range of pressure, temperature, catalyst concentration, and agitation rates. The reaction follows a pseudo-first-order course with a surface-reaction-controlling step between atomically adsorbed hydrogen and adsorbed xylose at 100° and unadsorbed xylose at higher temperatures.",

author = "J. Wisniak and M. Hershkowitz and R. Leibowitz and S. Stein",

year = "1974",

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AU - Wisniak, J.

AU - Hershkowitz, M.

AU - Leibowitz, R.

AU - Stein, S.

PY - 1974/3/1

Y1 - 1974/3/1

N2 - Xylose has been hydrogenated with Raney nickel under a wide range of pressure, temperature, catalyst concentration, and agitation rates. The reaction follows a pseudo-first-order course with a surface-reaction-controlling step between atomically adsorbed hydrogen and adsorbed xylose at 100° and unadsorbed xylose at higher temperatures.

AB - Xylose has been hydrogenated with Raney nickel under a wide range of pressure, temperature, catalyst concentration, and agitation rates. The reaction follows a pseudo-first-order course with a surface-reaction-controlling step between atomically adsorbed hydrogen and adsorbed xylose at 100° and unadsorbed xylose at higher temperatures.

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JO - Industrial & Engineering Chemistry Product Research and Development

JF - Industrial & Engineering Chemistry Product Research and Development

IS - 1

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Hydrogenation of Xylose to Xylitol

Abstract

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