Measurement of interfacial areas with the chemical method for a system with alternating dispersed phases

B.A.A. van Woezik; K.R. Westerterp

doi:10.1016/S0255-2701(99)00089-6

Measurement of interfacial areas with the chemical method for a system with alternating dispersed phases

B.A.A. van Woezik
, K.R. Westerterp

Research output: Contribution to journal › Article › Academic › peer-review

26 Citations (Scopus)

18 Downloads (Pure)

Abstract

The interfacial area for a liquid–liquid system has been determined by the chemical reaction method. The saponification of butyl formate ester with 8 M sodium hydroxide has been used to this end. A correlation has been derived to describe the mole flux of ester through the interface and the kinetic rate constants have been calculated. For a continuously operated reactor a correlation has been derived for both reaction in the dispersed phase as well as reaction in the continuous phase. A viscosity factor had to be incorporated to obtain one single correlation for the Sauter mean drop diameter. The validation for this chemically enhanced reaction regime is presented and discussed.

Original language	Undefined
Pages (from-to)	299-314
Number of pages	16
Journal	Chemical engineering and processing : process intensification
Volume	39
Issue number	4
DOIs	https://doi.org/10.1016/S0255-2701(99)00089-6
Publication status	Published - 2000

Keywords

METIS-106086
IR-74310
Saponification
Fast liquid–liquid reaction
Heterogeneous dispersion
Interfacial area
Butyl formate ester
Chemical reaction method

Access to Document

10.1016/S0255-2701(99)00089-6

Cite this

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title = "Measurement of interfacial areas with the chemical method for a system with alternating dispersed phases",

abstract = "The interfacial area for a liquid–liquid system has been determined by the chemical reaction method. The saponification of butyl formate ester with 8 M sodium hydroxide has been used to this end. A correlation has been derived to describe the mole flux of ester through the interface and the kinetic rate constants have been calculated. For a continuously operated reactor a correlation has been derived for both reaction in the dispersed phase as well as reaction in the continuous phase. A viscosity factor had to be incorporated to obtain one single correlation for the Sauter mean drop diameter. The validation for this chemically enhanced reaction regime is presented and discussed.",

keywords = "METIS-106086, IR-74310, Saponification, Fast liquid–liquid reaction, Heterogeneous dispersion, Interfacial area, Butyl formate ester, Chemical reaction method",

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year = "2000",

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T1 - Measurement of interfacial areas with the chemical method for a system with alternating dispersed phases

AU - van Woezik, B.A.A.

AU - Westerterp, K.R.

PY - 2000

Y1 - 2000

N2 - The interfacial area for a liquid–liquid system has been determined by the chemical reaction method. The saponification of butyl formate ester with 8 M sodium hydroxide has been used to this end. A correlation has been derived to describe the mole flux of ester through the interface and the kinetic rate constants have been calculated. For a continuously operated reactor a correlation has been derived for both reaction in the dispersed phase as well as reaction in the continuous phase. A viscosity factor had to be incorporated to obtain one single correlation for the Sauter mean drop diameter. The validation for this chemically enhanced reaction regime is presented and discussed.

AB - The interfacial area for a liquid–liquid system has been determined by the chemical reaction method. The saponification of butyl formate ester with 8 M sodium hydroxide has been used to this end. A correlation has been derived to describe the mole flux of ester through the interface and the kinetic rate constants have been calculated. For a continuously operated reactor a correlation has been derived for both reaction in the dispersed phase as well as reaction in the continuous phase. A viscosity factor had to be incorporated to obtain one single correlation for the Sauter mean drop diameter. The validation for this chemically enhanced reaction regime is presented and discussed.

KW - METIS-106086

KW - IR-74310

KW - Saponification

KW - Fast liquid–liquid reaction

KW - Heterogeneous dispersion

KW - Interfacial area

KW - Butyl formate ester

KW - Chemical reaction method

U2 - 10.1016/S0255-2701(99)00089-6

DO - 10.1016/S0255-2701(99)00089-6

M3 - Article

SN - 0255-2701

VL - 39

SP - 299

EP - 314

JO - Chemical engineering and processing : process intensification

JF - Chemical engineering and processing : process intensification

IS - 4

ER -