Mass transfer and reaction rate in rotating solid foam reactors

R. Tschentscher; T.A. Nijhuis; J. Schaaf, van der; B.F.M. Kuster; J.C. Schouten

Mass transfer and reaction rate in rotating solid foam reactors

R. Tschentscher, T.A. Nijhuis, J. Schaaf, van der, B.F.M. Kuster, J.C. Schouten

Chemical Reactor Engineering

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

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Abstract

Reactor configurations based on rotating solid foams for fast three-phase reactions are presented. Solid foams are used as catalyst support and stirrer to mix the gas and liquid phases and to create fine gas bubbles. Mass transfer data are presented for different solid foam stirrer configurations and are compared to a slurry reactor with a Rushton stirrer. The foam block stirrer shows a kGLaGL of 0.18 s-1, which is 60% higher than using a Rushton stirrer. With a value of 4.2x10-3 ms-1 the liquid-solid mass transfer coefficient is around 20% higher than for the Rushton stirrer with copper slurry particles.

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	157-
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

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title = "Mass transfer and reaction rate in rotating solid foam reactors",

abstract = "Reactor configurations based on rotating solid foams for fast three-phase reactions are presented. Solid foams are used as catalyst support and stirrer to mix the gas and liquid phases and to create fine gas bubbles. Mass transfer data are presented for different solid foam stirrer configurations and are compared to a slurry reactor with a Rushton stirrer. The foam block stirrer shows a kGLaGL of 0.18 s-1, which is 60% higher than using a Rushton stirrer. With a value of 4.2x10-3 ms-1 the liquid-solid mass transfer coefficient is around 20% higher than for the Rushton stirrer with copper slurry particles.",

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

year = "2010",

language = "English",

pages = "157--",

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",

}

Tschentscher, R, Nijhuis, TA, Schaaf, van der, J, Kuster, BFM & Schouten, JC 2010, Mass transfer and reaction rate in rotating solid foam reactors. in Proceedings of the 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), 13-16 June 2010 Philadelphia United States. pp. 157-, 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), Philadelphia, PA, United States, 13/06/10.

Mass transfer and reaction rate in rotating solid foam reactors. / Tschentscher, R.; Nijhuis, T.A.; Schaaf, van der, J.; Kuster, B.F.M.; Schouten, J.C.

Proceedings of the 21st International Symposium on Chemical Reaction Engineering (ISCRE 21), 13-16 June 2010 Philadelphia United States. 2010. p. 157-.

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

TY - GEN

T1 - Mass transfer and reaction rate in rotating solid foam reactors

AU - Tschentscher, R.

AU - Nijhuis, T.A.

AU - Schaaf, van der, J.

AU - Kuster, B.F.M.

AU - Schouten, J.C.

PY - 2010

Y1 - 2010

N2 - Reactor configurations based on rotating solid foams for fast three-phase reactions are presented. Solid foams are used as catalyst support and stirrer to mix the gas and liquid phases and to create fine gas bubbles. Mass transfer data are presented for different solid foam stirrer configurations and are compared to a slurry reactor with a Rushton stirrer. The foam block stirrer shows a kGLaGL of 0.18 s-1, which is 60% higher than using a Rushton stirrer. With a value of 4.2x10-3 ms-1 the liquid-solid mass transfer coefficient is around 20% higher than for the Rushton stirrer with copper slurry particles.

AB - Reactor configurations based on rotating solid foams for fast three-phase reactions are presented. Solid foams are used as catalyst support and stirrer to mix the gas and liquid phases and to create fine gas bubbles. Mass transfer data are presented for different solid foam stirrer configurations and are compared to a slurry reactor with a Rushton stirrer. The foam block stirrer shows a kGLaGL of 0.18 s-1, which is 60% higher than using a Rushton stirrer. With a value of 4.2x10-3 ms-1 the liquid-solid mass transfer coefficient is around 20% higher than for the Rushton stirrer with copper slurry particles.

M3 - Conference contribution

SP - 157-

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 -

Mass transfer and reaction rate in rotating solid foam reactors

Abstract

Conference

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