Liquid-solid mass transfer in a rotor-stator spinning disc reactor

M. Meeuwse; J. Schaaf, van der; J.C. Schouten

Liquid-solid mass transfer in a rotor-stator spinning disc reactor

M. Meeuwse
, J. Schaaf, van der
, J.C. Schouten

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

2 Downloads (Pure)

Abstract

Liquid-solid mass transfer coefficients in a rotor-stator spinning disc reactor are reported that were determined from measurements of reaction rates of the heterogeneously catalysed oxidation of glucose.The overall reaction rates are limited by both liquid-solid mass transfer and the intrinsic oxidation kinetics at the operating conditions used. The liquid-solid mass transfer increases with increasing rotational disc speed. The estimated liquid-solid mass transfer coefficient kLS increases from 1.5 · 10-4 m s-1 at 49 rad s-1 to 3 · 10-4 m s-1 at 181 rad s-1, which is at least a factor 3 higher than in conventional reactors.

Original language	English
Title of host publication	Proceedings of the 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), 13-16 June 2010 Philadelphia United States
Pages	Abstract 121-
Publication status	Published - 2010
Event	21st International Symposium on Chemical Reaction Engineering (ISCRE 21) - Philadelphia, PA, United States Duration: 13 Jun 2010 → 16 Jun 2010

Conference

Conference	21st International Symposium on Chemical Reaction Engineering (ISCRE 21)
Abbreviated title	ISCRE 21
Country/Territory	United States
City	Philadelphia, PA
Period	13/06/10 → 16/06/10

Cite this

@inproceedings{d9a049027c5245769c4b7a09b1c0c836,

title = "Liquid-solid mass transfer in a rotor-stator spinning disc reactor",

abstract = "Liquid-solid mass transfer coefficients in a rotor-stator spinning disc reactor are reported that were determined from measurements of reaction rates of the heterogeneously catalysed oxidation of glucose.The overall reaction rates are limited by both liquid-solid mass transfer and the intrinsic oxidation kinetics at the operating conditions used. The liquid-solid mass transfer increases with increasing rotational disc speed. The estimated liquid-solid mass transfer coefficient kLS increases from 1.5 · 10-4 m s-1 at 49 rad s-1 to 3 · 10-4 m s-1 at 181 rad s-1, which is at least a factor 3 higher than in conventional reactors.",

author = "M. Meeuwse and \{Schaaf, van der\}, J. and J.C. Schouten",

year = "2010",

language = "English",

pages = "Abstract 121--",

booktitle = "Proceedings of the 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), 13-16 June 2010 Philadelphia United States",

note = "21st International Symposium on Chemical Reaction Engineering (ISCRE 21), ISCRE 21 ; Conference date: 13-06-2010 Through 16-06-2010",

}

Meeuwse, M, Schaaf, van der, J & Schouten, JC 2010, Liquid-solid mass transfer in a rotor-stator spinning disc reactor. in Proceedings of the 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), 13-16 June 2010 Philadelphia United States. pp. Abstract 121-, 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), Philadelphia, PA, United States, 13/06/10.

Liquid-solid mass transfer in a rotor-stator spinning disc reactor. / Meeuwse, M.; Schaaf, van der, J.; Schouten, J.C.
Proceedings of the 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), 13-16 June 2010 Philadelphia United States. 2010. p. Abstract 121-.

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

TY - GEN

T1 - Liquid-solid mass transfer in a rotor-stator spinning disc reactor

AU - Meeuwse, M.

AU - Schaaf, van der, J.

AU - Schouten, J.C.

PY - 2010

Y1 - 2010

N2 - Liquid-solid mass transfer coefficients in a rotor-stator spinning disc reactor are reported that were determined from measurements of reaction rates of the heterogeneously catalysed oxidation of glucose.The overall reaction rates are limited by both liquid-solid mass transfer and the intrinsic oxidation kinetics at the operating conditions used. The liquid-solid mass transfer increases with increasing rotational disc speed. The estimated liquid-solid mass transfer coefficient kLS increases from 1.5 · 10-4 m s-1 at 49 rad s-1 to 3 · 10-4 m s-1 at 181 rad s-1, which is at least a factor 3 higher than in conventional reactors.

AB - Liquid-solid mass transfer coefficients in a rotor-stator spinning disc reactor are reported that were determined from measurements of reaction rates of the heterogeneously catalysed oxidation of glucose.The overall reaction rates are limited by both liquid-solid mass transfer and the intrinsic oxidation kinetics at the operating conditions used. The liquid-solid mass transfer increases with increasing rotational disc speed. The estimated liquid-solid mass transfer coefficient kLS increases from 1.5 · 10-4 m s-1 at 49 rad s-1 to 3 · 10-4 m s-1 at 181 rad s-1, which is at least a factor 3 higher than in conventional reactors.

M3 - Conference contribution

SP - Abstract 121-

BT - Proceedings of the 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), 13-16 June 2010 Philadelphia United States

T2 - 21st International Symposium on Chemical Reaction Engineering (ISCRE 21)

Y2 - 13 June 2010 through 16 June 2010

ER -

Liquid-solid mass transfer in a rotor-stator spinning disc reactor

Abstract

Conference

Fingerprint

Cite this