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

F. Visscher; J. Schaaf, van der; M.H.J.M. Croon, de; J.C. Schouten

doi:10.1016/j.cej.2012.01.002

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

F. Visscher, J. Schaaf, van der, M.H.J.M. Croon, de, J.C. Schouten

Chemical Reactor Engineering

Onderzoeksoutput: Bijdrage aan tijdschrift › Tijdschriftartikel › Academic › peer review

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The liquid–liquid flow behaviour and mass transfer rates for a rotor–stator spinning disc reactor are reported. The measured mass transfer rate is at least 25 times higher compared to packed column. This makes that the rotor–stator spinning disc reactor is a promising multiphase reactor.

Originele taal-2	Engels
Pagina's (van-tot)	267-243
Aantal pagina's	7
Tijdschrift	Chemical Engineering Journal
Volume	185-186
DOI's	https://doi.org/10.1016/j.cej.2012.01.002
Status	Gepubliceerd - 2012

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10.1016/j.cej.2012.01.002

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@article{8b92082444fa4a06a0a2e96580efc51b,

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

abstract = "The liquid–liquid flow behaviour and mass transfer rates for a rotor–stator spinning disc reactor are reported. The measured mass transfer rate is at least 25 times higher compared to packed column. This makes that the rotor–stator spinning disc reactor is a promising multiphase reactor.",

author = "F. Visscher and {Schaaf, van der}, J. and {Croon, de}, M.H.J.M. and J.C. Schouten",

year = "2012",

doi = "10.1016/j.cej.2012.01.002",

language = "English",

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AU - Visscher, F.

AU - Schaaf, van der, J.

AU - Croon, de, M.H.J.M.

AU - Schouten, J.C.

PY - 2012

Y1 - 2012

N2 - The liquid–liquid flow behaviour and mass transfer rates for a rotor–stator spinning disc reactor are reported. The measured mass transfer rate is at least 25 times higher compared to packed column. This makes that the rotor–stator spinning disc reactor is a promising multiphase reactor.

AB - The liquid–liquid flow behaviour and mass transfer rates for a rotor–stator spinning disc reactor are reported. The measured mass transfer rate is at least 25 times higher compared to packed column. This makes that the rotor–stator spinning disc reactor is a promising multiphase reactor.

U2 - 10.1016/j.cej.2012.01.002

DO - 10.1016/j.cej.2012.01.002

M3 - Article

SN - 1385-8947

VL - 185-186

SP - 267

EP - 243

JO - Chemical Engineering Journal

JF - Chemical Engineering Journal

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

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