LrgpV1, PascalFrancis, Corpus, bibRecord, 000708

Rheology and heat transfer during mineral residue phosphatation in a rheo-reactor

Identifieur interne : 000708 ( PascalFrancis/Corpus ); précédent : 000707; suivant : 000709

Rheology and heat transfer during mineral residue phosphatation in a rheo-reactor

Auteurs : A. Nzihou ; B. Bournonville ; P. Marchal ; L. Choplin

Source :

Chemical engineering research & design [ 0263-8762 ] ; 2004.

RBID : Pascal:04-0428842

Descripteurs français

Pascal (Inist)
- Transfert chaleur, Phosphatation, Réacteur, Agitateur ruban, Viscosité, Analyse quantitative, Macromélangeage, Dissipation visqueuse, Nombre Nusselt, Coefficient transfert chaleur.

English descriptors

KwdEn :
- Heat transfer, Heat transfer coefficient, Macromixing, Nusselt number, Phosphating, Quantitative analysis, Reactor, Ribbon agitator, Viscosity, Viscous dissipation.

Abstract

The rheo-reactor consists of a cylindrical vessel equipped with a double helical ribbon impeller installed in a RS150 controlled stress rheometer. It was used to investigate the rheological behaviour and the heat transfer in aqueous mineral residue suspensions during the phosphatation process. The absolute viscosity was determined using a Couette analogy allowing the quantitative analysis of the torque-rotational speed. The results show that the suspensions exhibit a viscoplastic or Binghamian behavior. The experimental operating conditions for the phosphatation process were then selected in order to ensure a good macromixing, even in laminar regime (Re < 30). Heat was generated as the combined result of the exothermic phosphatation process and the viscous dissipation inside the rheo-reactor. The heat produced needed to be efficiently removed to reduce its effect on the behaviour of the suspension. This was evaluated using the Nusselt number and the heat transfer coefficient h.

Notice en format standard (ISO 2709)

Pour connaître la documentation sur le format Inist Standard.

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A02	`01`			`@0 CERDEE`
A03		`1`		`@0 Chem. eng. res. des.`
A05				`@2 82`
A06				`@2 5`
A08	`01`	`1`	`ENG`	`@1 Rheology and heat transfer during mineral residue phosphatation in a rheo-reactor`
A11	`01`	`1`		`@1 NZIHOU (A.)`
A11	`02`	`1`		`@1 BOURNONVILLE (B.)`
A11	`03`	`1`		`@1 MARCHAL (P.)`
A11	`04`	`1`		`@1 CHOPLIN (L.)`
A14	`01`			`@1 LGPSD, UMR CNRS 2392, Ecole des Mines d'Albi-Carmaux @2 Albi @3 FRA @Z 1 aut. @Z 2 aut.`
A14	`02`			`@1 Francc GEMICO, ENSIC @2 Nancy @3 FRA @Z 3 aut. @Z 4 aut.`
A20				`@1 637-641`
A21				`@1 2004`
A23	`01`			`@0 ENG`
A43	`01`			`@1 INIST @2 4284 @5 354000110309300100`
A44				`@0 0000 @1 © 2004 INIST-CNRS. All rights reserved.`
A45				`@0 14 ref.`
A47	`01`	`1`		`@0 04-0428842`
A60				`@1 P`
A61				`@0 A`
A64	`01`	`1`		`@0 Chemical engineering research & design`
A66	`01`			`@0 GBR`
C01	`01`		`ENG`	@0 The rheo-reactor consists of a cylindrical vessel equipped with a double helical ribbon impeller installed in a RS150 controlled stress rheometer. It was used to investigate the rheological behaviour and the heat transfer in aqueous mineral residue suspensions during the phosphatation process. The absolute viscosity was determined using a Couette analogy allowing the quantitative analysis of the torque-rotational speed. The results show that the suspensions exhibit a viscoplastic or Binghamian behavior. The experimental operating conditions for the phosphatation process were then selected in order to ensure a good macromixing, even in laminar regime (Re < 30). Heat was generated as the combined result of the exothermic phosphatation process and the viscous dissipation inside the rheo-reactor. The heat produced needed to be efficiently removed to reduce its effect on the behaviour of the suspension. This was evaluated using the Nusselt number and the heat transfer coefficient h.
C02	`01`	`X`		`@0 001D07G`
C02	`02`	`X`		`@0 001D07H`
C03	`01`	`X`	`FRE`	`@0 Transfert chaleur @5 01`
C03	`01`	`X`	`ENG`	`@0 Heat transfer @5 01`
C03	`01`	`X`	`SPA`	`@0 Transferencia térmica @5 01`
C03	`02`	`X`	`FRE`	`@0 Phosphatation @5 02`
C03	`02`	`X`	`ENG`	`@0 Phosphating @5 02`
C03	`02`	`X`	`SPA`	`@0 Fosfatación @5 02`
C03	`03`	`X`	`FRE`	`@0 Réacteur @5 03`
C03	`03`	`X`	`ENG`	`@0 Reactor @5 03`
C03	`03`	`X`	`SPA`	`@0 Reactor @5 03`
C03	`04`	`X`	`FRE`	`@0 Agitateur ruban @5 04`
C03	`04`	`X`	`ENG`	`@0 Ribbon agitator @5 04`
C03	`04`	`X`	`SPA`	`@0 Agitador cinta @5 04`
C03	`05`	`X`	`FRE`	`@0 Viscosité @5 05`
C03	`05`	`X`	`ENG`	`@0 Viscosity @5 05`
C03	`05`	`X`	`SPA`	`@0 Viscosidad @5 05`
C03	`06`	`X`	`FRE`	`@0 Analyse quantitative @5 06`
C03	`06`	`X`	`ENG`	`@0 Quantitative analysis @5 06`
C03	`06`	`X`	`SPA`	`@0 Análisis cuantitativo @5 06`
C03	`07`	`X`	`FRE`	`@0 Macromélangeage @5 07`
C03	`07`	`X`	`ENG`	`@0 Macromixing @5 07`
C03	`07`	`X`	`SPA`	`@0 Macromezcla @5 07`
C03	`08`	`X`	`FRE`	`@0 Dissipation visqueuse @5 08`
C03	`08`	`X`	`ENG`	`@0 Viscous dissipation @5 08`
C03	`08`	`X`	`SPA`	`@0 Disipación viscosa @5 08`
C03	`09`	`X`	`FRE`	`@0 Nombre Nusselt @5 09`
C03	`09`	`X`	`ENG`	`@0 Nusselt number @5 09`
C03	`09`	`X`	`SPA`	`@0 Número Nusselt @5 09`
C03	`10`	`X`	`FRE`	`@0 Coefficient transfert chaleur @5 10`
C03	`10`	`X`	`ENG`	`@0 Heat transfer coefficient @5 10`
C03	`10`	`X`	`SPA`	`@0 Coeficiente transmisión calor @5 10`
N21				`@1 243`
N44	`01`			`@1 OTO`
N82				`@1 OTO`

Format Inist (serveur)

NO :	PASCAL 04-0428842 INIST
ET :	Rheology and heat transfer during mineral residue phosphatation in a rheo-reactor
AU :	NZIHOU (A.); BOURNONVILLE (B.); MARCHAL (P.); CHOPLIN (L.)
AF :	LGPSD, UMR CNRS 2392, Ecole des Mines d'Albi-Carmaux/Albi/France (1 aut., 2 aut.); Francc GEMICO, ENSIC/Nancy/France (3 aut., 4 aut.)
DT :	Publication en série; Niveau analytique
SO :	Chemical engineering research & design; ISSN 0263-8762; Coden CERDEE; Royaume-Uni; Da. 2004; Vol. 82; No. 5; Pp. 637-641; Bibl. 14 ref.
LA :	Anglais
EA :	The rheo-reactor consists of a cylindrical vessel equipped with a double helical ribbon impeller installed in a RS150 controlled stress rheometer. It was used to investigate the rheological behaviour and the heat transfer in aqueous mineral residue suspensions during the phosphatation process. The absolute viscosity was determined using a Couette analogy allowing the quantitative analysis of the torque-rotational speed. The results show that the suspensions exhibit a viscoplastic or Binghamian behavior. The experimental operating conditions for the phosphatation process were then selected in order to ensure a good macromixing, even in laminar regime (Re < 30). Heat was generated as the combined result of the exothermic phosphatation process and the viscous dissipation inside the rheo-reactor. The heat produced needed to be efficiently removed to reduce its effect on the behaviour of the suspension. This was evaluated using the Nusselt number and the heat transfer coefficient h.
CC :	001D07G; 001D07H
FD :	Transfert chaleur; Phosphatation; Réacteur; Agitateur ruban; Viscosité; Analyse quantitative; Macromélangeage; Dissipation visqueuse; Nombre Nusselt; Coefficient transfert chaleur
ED :	Heat transfer; Phosphating; Reactor; Ribbon agitator; Viscosity; Quantitative analysis; Macromixing; Viscous dissipation; Nusselt number; Heat transfer coefficient
SD :	Transferencia térmica; Fosfatación; Reactor; Agitador cinta; Viscosidad; Análisis cuantitativo; Macromezcla; Disipación viscosa; Número Nusselt; Coeficiente transmisión calor
LO :	INIST-4284.354000110309300100
ID :	04-0428842

Links to Exploration step

Pascal:04-0428842

Le document en format XML

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<front><div type="abstract" xml:lang="en">The rheo-reactor consists of a cylindrical vessel equipped with a double helical ribbon impeller installed in a RS150 controlled stress rheometer. It was used to investigate the rheological behaviour and the heat transfer in aqueous mineral residue suspensions during the phosphatation process. The absolute viscosity was determined using a Couette analogy allowing the quantitative analysis of the torque-rotational speed. The results show that the suspensions exhibit a viscoplastic or Binghamian behavior. The experimental operating conditions for the phosphatation process were then selected in order to ensure a good macromixing, even in laminar regime (Re < 30). Heat was generated as the combined result of the exothermic phosphatation process and the viscous dissipation inside the rheo-reactor. The heat produced needed to be efficiently removed to reduce its effect on the behaviour of the suspension. This was evaluated using the Nusselt number and the heat transfer coefficient h.</div>
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<server><NO>PASCAL 04-0428842 INIST</NO>
<ET>Rheology and heat transfer during mineral residue phosphatation in a rheo-reactor</ET>
<AU>NZIHOU (A.); BOURNONVILLE (B.); MARCHAL (P.); CHOPLIN (L.)</AU>
<AF>LGPSD, UMR CNRS 2392, Ecole des Mines d'Albi-Carmaux/Albi/France (1 aut., 2 aut.); Francc GEMICO, ENSIC/Nancy/France (3 aut., 4 aut.)</AF>
<DT>Publication en série; Niveau analytique</DT>
<SO>Chemical engineering research & design; ISSN 0263-8762; Coden CERDEE; Royaume-Uni; Da. 2004; Vol. 82; No. 5; Pp. 637-641; Bibl. 14 ref.</SO>
<LA>Anglais</LA>
<EA>The rheo-reactor consists of a cylindrical vessel equipped with a double helical ribbon impeller installed in a RS150 controlled stress rheometer. It was used to investigate the rheological behaviour and the heat transfer in aqueous mineral residue suspensions during the phosphatation process. The absolute viscosity was determined using a Couette analogy allowing the quantitative analysis of the torque-rotational speed. The results show that the suspensions exhibit a viscoplastic or Binghamian behavior. The experimental operating conditions for the phosphatation process were then selected in order to ensure a good macromixing, even in laminar regime (Re < 30). Heat was generated as the combined result of the exothermic phosphatation process and the viscous dissipation inside the rheo-reactor. The heat produced needed to be efficiently removed to reduce its effect on the behaviour of the suspension. This was evaluated using the Nusselt number and the heat transfer coefficient h.</EA>
<CC>001D07G; 001D07H</CC>
<FD>Transfert chaleur; Phosphatation; Réacteur; Agitateur ruban; Viscosité; Analyse quantitative; Macromélangeage; Dissipation visqueuse; Nombre Nusselt; Coefficient transfert chaleur</FD>
<ED>Heat transfer; Phosphating; Reactor; Ribbon agitator; Viscosity; Quantitative analysis; Macromixing; Viscous dissipation; Nusselt number; Heat transfer coefficient</ED>
<SD>Transferencia térmica; Fosfatación; Reactor; Agitador cinta; Viscosidad; Análisis cuantitativo; Macromezcla; Disipación viscosa; Número Nusselt; Coeficiente transmisión calor</SD>
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<ID>04-0428842</ID>
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Rheology and heat transfer during mineral residue phosphatation in a rheo-reactor

Rheology and heat transfer during mineral residue phosphatation in a rheo-reactor

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