Residence time distribution of the gas phase in a mechanically agitated gas-liquid reactor

M.P.G. Thijert; M.H. Oyevaar; W.J. Kuper; K.R. Westerterp

doi:10.1016/0009-2509(92)85043-B

Residence time distribution of the gas phase in a mechanically agitated gas-liquid reactor

M.P.G. Thijert, M.H. Oyevaar, W.J. Kuper, K.R. Westerterp

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Abstract

In this study we present a measuring method and extensive experimental data on the gas phase RTD in a mechanically agitated gas-liquid reactor with standard dimensions over a wide range of superficial gas velocities, agitation rates and agitator sizes. The results are modelled successfully, using the weighed moments method, by a simple RTD model of one mixer in series with a plug flow zone. All results are correlated in one relation, which can be used for scale-up.

Original language	Undefined
Pages (from-to)	3339-3346
Number of pages	8
Journal	Chemical engineering science
Volume	47
Issue number	13
DOIs	https://doi.org/10.1016/0009-2509(92)85043-B
Publication status	Published - 1992

Keywords

METIS-105844
IR-10801

Access to Document

10.1016/0009-2509(92)85043-B

Thijert92residence

Cite this

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abstract = "In this study we present a measuring method and extensive experimental data on the gas phase RTD in a mechanically agitated gas-liquid reactor with standard dimensions over a wide range of superficial gas velocities, agitation rates and agitator sizes. The results are modelled successfully, using the weighed moments method, by a simple RTD model of one mixer in series with a plug flow zone. All results are correlated in one relation, which can be used for scale-up.",

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AU - Thijert, M.P.G.

AU - Oyevaar, M.H.

AU - Kuper, W.J.

AU - Westerterp, K.R.

PY - 1992

Y1 - 1992

N2 - In this study we present a measuring method and extensive experimental data on the gas phase RTD in a mechanically agitated gas-liquid reactor with standard dimensions over a wide range of superficial gas velocities, agitation rates and agitator sizes. The results are modelled successfully, using the weighed moments method, by a simple RTD model of one mixer in series with a plug flow zone. All results are correlated in one relation, which can be used for scale-up.

AB - In this study we present a measuring method and extensive experimental data on the gas phase RTD in a mechanically agitated gas-liquid reactor with standard dimensions over a wide range of superficial gas velocities, agitation rates and agitator sizes. The results are modelled successfully, using the weighed moments method, by a simple RTD model of one mixer in series with a plug flow zone. All results are correlated in one relation, which can be used for scale-up.

KW - METIS-105844

KW - IR-10801

U2 - 10.1016/0009-2509(92)85043-B

DO - 10.1016/0009-2509(92)85043-B

M3 - Article

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JO - Chemical engineering science

JF - Chemical engineering science

SN - 0009-2509

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