LrgpV1, Istex, Corpus, bibRecord, 000067

A complete model for oxidation air-lift reactors

Identifieur interne : 000067 ( Istex/Corpus ); précédent : 000066; suivant : 000068

A complete model for oxidation air-lift reactors

Auteurs : E. Camarasa ; L. A. C. Meleiro ; E. Carvalho ; A. Domingues ; R. Maciel Filho ; G. Wild ; S. Poncin ; N. Midoux ; J. Bouillard

Source :

Computers and Chemical Engineering [ 0098-1354 ] ; 2001.

RBID : ISTEX:3B0E6A639017B79BD7BD0DCD44E610FD05D0BDCE

English descriptors

KwdEn :
- Adequate model, Airlift reactor, Airlift reactors, Balance equations, Bubble column reactors, Bubble diameter, Camarasa, Cell model, Cell number, Chemical engineering, Chemical engineering science, Chemical reaction, Cmbf, Complete model, Downcomer, Elsevier science, Energy balance, Enhancement factor, Experimental data, Gas hold-up, Heterogeneous regime, Homogeneous regime, Hydrodynamic, Hydrodynamic model, Hydrodynamic parameters, Hydrodynamics, Hydrodynamics parameters, Industrial system, Inert component, Interfacial area, Kinetics, Liquid bulk, Liquid circulation, Liquid circulation velocity, Liquid density, Liquid phase, Liquid phases, Liquid velocity, Local pressure, Maciel filho, Mass balance, Mass balances, Mass transfer, Modeling, Momentum balance, Organic products, Oxidation reactor, Oxidation reactors, Oxygen absorption, Oxygen absorption rate, Oxygen balance, Peclet number, Pilot plant, Reaction kinetics, Reactor, Reactor geometry, Rhodia brasil, Riser, Riser height, Schematic description, Total pressure drop.
Teeft :
- Adequate model, Airlift reactors, Balance equations, Bubble column reactors, Bubble diameter, Camarasa, Cell model, Cell number, Chemical engineering, Chemical engineering science, Chemical reaction, Cmbf, Complete model, Downcomer, Elsevier science, Energy balance, Enhancement factor, Experimental data, Heterogeneous regime, Homogeneous regime, Hydrodynamic, Hydrodynamic model, Hydrodynamic parameters, Hydrodynamics, Hydrodynamics parameters, Industrial system, Inert component, Interfacial area, Kinetics, Liquid bulk, Liquid circulation, Liquid circulation velocity, Liquid density, Liquid phase, Liquid phases, Liquid velocity, Local pressure, Maciel filho, Mass balance, Mass balances, Mass transfer, Momentum balance, Organic products, Oxidation reactor, Oxidation reactors, Oxygen absorption, Oxygen absorption rate, Oxygen balance, Peclet number, Pilot plant, Reaction kinetics, Reactor, Reactor geometry, Rhodia brasil, Riser, Riser height, Schematic description, Total pressure drop.

Abstract

Abstract: A complete model for prediction performance of an oxidation air-lift reactor has been developed. The model includes reaction kinetics, flow configuration, mass transfer and hydrodynamics. Liquid bulk and gas phases are modeled using a cell model. The mass transfer rates are computed from the film model. Hydrodynamics parameters are calculated with an adequate model based on balance equations and on experimental data. The model predicts the variations of concentrations and hydrodynamics parameters along the reactor and hence is able to provide a good description of the reactor.

Url:

https://api.istex.fr/document/3B0E6A639017B79BD7BD0DCD44E610FD05D0BDCE/fulltext/pdf

DOI: 10.1016/S0098-1354(01)00637-8

Links to Exploration step

ISTEX:3B0E6A639017B79BD7BD0DCD44E610FD05D0BDCE

Le document en format XML

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<front><div type="abstract" xml:lang="en">Abstract: A complete model for prediction performance of an oxidation air-lift reactor has been developed. The model includes reaction kinetics, flow configuration, mass transfer and hydrodynamics. Liquid bulk and gas phases are modeled using a cell model. The mass transfer rates are computed from the film model. Hydrodynamics parameters are calculated with an adequate model based on balance equations and on experimental data. The model predicts the variations of concentrations and hydrodynamics parameters along the reactor and hence is able to provide a good description of the reactor.</div>
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<notesStmt><note type="content">Fig. 1: Schematic description of the air-lift model.</note>
<note type="content">Fig. 2: Description of the cell model.</note>
<note type="content">Fig. 3: Description of the hydrodynamic model.</note>
<note type="content">Fig. 4: (a) Variation of gas hold-up in the riser. (b) Variation of bubble diameter and gas–liquid interfacial area in the riser.</note>
<note type="content">Fig. 5: Profiles of component B and P along the riser.</note>
<note type="content">Fig. 6: Profiles of O2 in liquid and gas phases.</note>
<note type="content">Fig. 7: Variation of E and Ha with riser height.</note>
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<abstract xml:lang="en"><p>A complete model for prediction performance of an oxidation air-lift reactor has been developed. The model includes reaction kinetics, flow configuration, mass transfer and hydrodynamics. Liquid bulk and gas phases are modeled using a cell model. The mass transfer rates are computed from the film model. Hydrodynamics parameters are calculated with an adequate model based on balance equations and on experimental data. The model predicts the variations of concentrations and hydrodynamics parameters along the reactor and hence is able to provide a good description of the reactor.</p>
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<head><ce:title>A complete model for oxidation air-lift reactors</ce:title>
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<ce:abstract-sec><ce:simple-para>A complete model for prediction performance of an oxidation air-lift reactor has been developed. The model includes reaction kinetics, flow configuration, mass transfer and hydrodynamics. Liquid bulk and gas phases are modeled using a cell model. The mass transfer rates are computed from the film model. Hydrodynamics parameters are calculated with an adequate model based on balance equations and on experimental data. The model predicts the variations of concentrations and hydrodynamics parameters along the reactor and hence is able to provide a good description of the reactor.</ce:simple-para>
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<ce:keyword><ce:text>Airlift reactor</ce:text>
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<ce:keyword><ce:text>Mass transfer</ce:text>
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<abstract lang="en">Abstract: A complete model for prediction performance of an oxidation air-lift reactor has been developed. The model includes reaction kinetics, flow configuration, mass transfer and hydrodynamics. Liquid bulk and gas phases are modeled using a cell model. The mass transfer rates are computed from the film model. Hydrodynamics parameters are calculated with an adequate model based on balance equations and on experimental data. The model predicts the variations of concentrations and hydrodynamics parameters along the reactor and hence is able to provide a good description of the reactor.</abstract>
<note type="content">Fig. 1: Schematic description of the air-lift model.</note>
<note type="content">Fig. 2: Description of the cell model.</note>
<note type="content">Fig. 3: Description of the hydrodynamic model.</note>
<note type="content">Fig. 4: (a) Variation of gas hold-up in the riser. (b) Variation of bubble diameter and gas–liquid interfacial area in the riser.</note>
<note type="content">Fig. 5: Profiles of component B and P along the riser.</note>
<note type="content">Fig. 6: Profiles of O2 in liquid and gas phases.</note>
<note type="content">Fig. 7: Variation of E and Ha with riser height.</note>
<subject lang="en"><genre>Keywords</genre>
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A complete model for oxidation air-lift reactors

A complete model for oxidation air-lift reactors

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