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

Onderzoeksoutput: Hoofdstuk in Boek/Rapport/Congresprocedure › Conferentiebijdrage › Academic › peer review

3 Downloads (Pure)

Samenvatting

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.

Originele taal-2	Engels
Titel	Proceedings of the 22nd North American Catalysis Society Meeting, 5-10 June 2011, Detroit, MI, USA
Pagina's	P-Mo-155-
Status	Gepubliceerd - 2011

Citeer dit

@inproceedings{c9d794e95a2c42c29f5b6ac65293ee7d,

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",

pages = "P--Mo--155--",

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

}

TY - GEN

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

Samenvatting

Vingerafdruk

Citeer dit