Glucose oxidation in rotating foam reactors

T.A. Nijhuis; R. Tschentscher; J. Schaaf, van der; J.C. Schouten

Glucose oxidation in rotating foam reactors

T.A. Nijhuis, R. Tschentscher, J. Schaaf, van der, J.C. Schouten

Chemical Reactor Engineering

Research output: Chapter in Book/Report/Conference proceeding › Conference contribution › Academic › peer-review

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Abstract

The mass transfer and reaction rates of rotating solid foam reactors were compared to a slurry reactor using the oxidation of glucose as a three-phase model reaction. Using the kinetic and mass transfer parameters the process conditions and the catalytic stirrer geometry have been optimized.

Original language	English
Title of host publication	Proceedings of the 22nd North American Catalysis Society Meeting, 5-10 June 2011, Detroit, MI, USA
Pages	P-Mo-155-
Publication status	Published - 2011

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title = "Glucose oxidation in rotating foam reactors",

abstract = "The mass transfer and reaction rates of rotating solid foam reactors were compared to a slurry reactor using the oxidation of glucose as a three-phase model reaction. Using the kinetic and mass transfer parameters the process conditions and the catalytic stirrer geometry have been optimized.",

author = "T.A. Nijhuis and R. Tschentscher and {Schaaf, van der}, J. and J.C. Schouten",

year = "2011",

language = "English",

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booktitle = "Proceedings of the 22nd North American Catalysis Society Meeting, 5-10 June 2011, Detroit, MI, USA",

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T1 - Glucose oxidation in rotating foam reactors

AU - Nijhuis, T.A.

AU - Tschentscher, R.

AU - Schaaf, van der, J.

AU - Schouten, J.C.

PY - 2011

Y1 - 2011

N2 - The mass transfer and reaction rates of rotating solid foam reactors were compared to a slurry reactor using the oxidation of glucose as a three-phase model reaction. Using the kinetic and mass transfer parameters the process conditions and the catalytic stirrer geometry have been optimized.

AB - The mass transfer and reaction rates of rotating solid foam reactors were compared to a slurry reactor using the oxidation of glucose as a three-phase model reaction. Using the kinetic and mass transfer parameters the process conditions and the catalytic stirrer geometry have been optimized.

M3 - Conference contribution

SP - P-Mo-155-

BT - Proceedings of the 22nd North American Catalysis Society Meeting, 5-10 June 2011, Detroit, MI, USA

ER -

Glucose oxidation in rotating foam reactors

Abstract

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