LrgpV1, PascalFrancis, Curation, bibRecord, 000937

Numerical study of evaporation in a vertical annulus heated at the inner wall

Identifieur interne : 000937 ( PascalFrancis/Curation ); précédent : 000936; suivant : 000938

Numerical study of evaporation in a vertical annulus heated at the inner wall

Auteurs : R. Ben Radhia [Tunisie] ; J. P. Corriou [France] ; S. Harmand [France] ; S. Ben Jabrallah [Tunisie]

Source :

International journal of thermal sciences [ 1290-0729 ] ; 2011.

RBID : Pascal:11-0459437

Descripteurs français

Pascal (Inist)
- Convection mixte, Eau, Film tombant, Cylindre vertical, Espace annulaire, Méthode volume fini, Modélisation, Simulation numérique, Evaporation, Transfert chaleur masse, Nombre Nusselt, Cylindre coaxial, Refroidissement évaporation.
Wicri :
- topic : Eau.

English descriptors

KwdEn :
- Annular space, Coaxial cylinders, Combined convection, Evaporation, Evaporative cooling, Falling film, Finite volume method, Heat mass transfer, Modeling, Numerical simulation, Nusselt number, Vertical cylinder, Water.

Abstract

Mixed convection during evaporation of a water falling film in a vertical concentric annulus was studied numerically. The water thin film falls on the inner tube and is subjected to a constant heat flux density, whereas the outer cylinder is assumed to be insulated and dry. An imposed air flow circulates within the gap between the two concentric tubes. The objective of this work is to understand the evaporation phenomenon in order to improve the average evaporated mass flux density and heat and mass transfer. Conservative equations governing the gas phase are solved numerically using the finite volume method. In the liquid phase, a method based on local heat and mass balances on each level is used. Thus, the following liquid film parameters, feed water mass flow, feed temperature and heat flux density, are taken into account. The obtained results are analyzed to emphasize and evaluate the influence of the previous operating parameters and the annulus curvature on the effective evaporation surface and on the mass flux density of evaporated water.

A01	`01`	`1`		`@0 1290-0729`
A03		`1`		`@0 Int. j. therm. sci.`
A05				`@2 50`
A06				`@2 10`
A08	`01`	`1`	`ENG`	`@1 Numerical study of evaporation in a vertical annulus heated at the inner wall`
A11	`01`	`1`		`@1 BEN RADHIA (R.)`
A11	`02`	`1`		`@1 CORRIOU (J. P.)`
A11	`03`	`1`		`@1 HARMAND (S.)`
A11	`04`	`1`		`@1 BEN JABRALLAH (S.)`
A14	`01`			`@1 Laboratoire d'Energétique et des Transferts Thermique et Massique, Faculté des Sciences de Tunis, Université Tunis El Manar @2 1060 Tunis @3 TUN @Z 1 aut. @Z 4 aut.`
A14	`02`			`@1 Faculté des sciences de Bizerte, Universite du 7 Novembreá Carthage @2 7021 Bizerte @3 TUN @Z 4 aut.`
A14	`03`			`@1 LRGP, Nancy Université, CNRS-ENSIC-INPL, 1 rue Grandville, BP 20451 @2 54001 Nancy @3 FRA @Z 2 aut.`
A14	`04`			`@1 Université de Lille Nord de France, F-59000 Lille UVHC/TEMPO @2 59313 Valenciennes @3 FRA @Z 3 aut.`
A20				`@1 1996-2005`
A21				`@1 2011`
A23	`01`			`@0 ENG`
A43	`01`			`@1 INIST @2 5065 @5 354000500129630200`
A44				`@0 0000 @1 © 2011 INIST-CNRS. All rights reserved.`
A45				`@0 25 ref.`
A47	`01`	`1`		`@0 11-0459437`
A60				`@1 P`
A61				`@0 A`
A64	`01`	`1`		`@0 International journal of thermal sciences`
A66	`01`			`@0 GBR`
C01	`01`		`ENG`	@0 Mixed convection during evaporation of a water falling film in a vertical concentric annulus was studied numerically. The water thin film falls on the inner tube and is subjected to a constant heat flux density, whereas the outer cylinder is assumed to be insulated and dry. An imposed air flow circulates within the gap between the two concentric tubes. The objective of this work is to understand the evaporation phenomenon in order to improve the average evaporated mass flux density and heat and mass transfer. Conservative equations governing the gas phase are solved numerically using the finite volume method. In the liquid phase, a method based on local heat and mass balances on each level is used. Thus, the following liquid film parameters, feed water mass flow, feed temperature and heat flux density, are taken into account. The obtained results are analyzed to emphasize and evaluate the influence of the previous operating parameters and the annulus curvature on the effective evaporation surface and on the mass flux density of evaporated water.
C02	`01`	`X`		`@0 001D06D02B`
C02	`02`	`X`		`@0 230`
C03	`01`	`X`	`FRE`	`@0 Convection mixte @5 02`
C03	`01`	`X`	`ENG`	`@0 Combined convection @5 02`
C03	`01`	`X`	`SPA`	`@0 Convección mixta @5 02`
C03	`02`	`X`	`FRE`	`@0 Eau @5 06`
C03	`02`	`X`	`ENG`	`@0 Water @5 06`
C03	`02`	`X`	`SPA`	`@0 Agua @5 06`
C03	`03`	`X`	`FRE`	`@0 Film tombant @5 08`
C03	`03`	`X`	`ENG`	`@0 Falling film @5 08`
C03	`03`	`X`	`SPA`	`@0 Película caediza @5 08`
C03	`04`	`X`	`FRE`	`@0 Cylindre vertical @5 09`
C03	`04`	`X`	`ENG`	`@0 Vertical cylinder @5 09`
C03	`04`	`X`	`SPA`	`@0 Cilindro vertical @5 09`
C03	`05`	`X`	`FRE`	`@0 Espace annulaire @5 10`
C03	`05`	`X`	`ENG`	`@0 Annular space @5 10`
C03	`05`	`X`	`SPA`	`@0 Espacio anular @5 10`
C03	`06`	`X`	`FRE`	`@0 Méthode volume fini @5 12`
C03	`06`	`X`	`ENG`	`@0 Finite volume method @5 12`
C03	`06`	`X`	`SPA`	`@0 Método volumen finito @5 12`
C03	`07`	`X`	`FRE`	`@0 Modélisation @5 15`
C03	`07`	`X`	`ENG`	`@0 Modeling @5 15`
C03	`07`	`X`	`SPA`	`@0 Modelización @5 15`
C03	`08`	`X`	`FRE`	`@0 Simulation numérique @5 16`
C03	`08`	`X`	`ENG`	`@0 Numerical simulation @5 16`
C03	`08`	`X`	`SPA`	`@0 Simulación numérica @5 16`
C03	`09`	`X`	`FRE`	`@0 Evaporation @5 23`
C03	`09`	`X`	`ENG`	`@0 Evaporation @5 23`
C03	`09`	`X`	`SPA`	`@0 Evaporación @5 23`
C03	`10`	`X`	`FRE`	`@0 Transfert chaleur masse @5 24`
C03	`10`	`X`	`ENG`	`@0 Heat mass transfer @5 24`
C03	`10`	`X`	`SPA`	`@0 Transferencia calor masa @5 24`
C03	`11`	`X`	`FRE`	`@0 Nombre Nusselt @5 25`
C03	`11`	`X`	`ENG`	`@0 Nusselt number @5 25`
C03	`11`	`X`	`SPA`	`@0 Número Nusselt @5 25`
C03	`12`	`X`	`FRE`	`@0 Cylindre coaxial @5 29`
C03	`12`	`X`	`ENG`	`@0 Coaxial cylinders @5 29`
C03	`12`	`X`	`SPA`	`@0 Cilindro coaxial @5 29`
C03	`13`	`X`	`FRE`	`@0 Refroidissement évaporation @5 30`
C03	`13`	`X`	`ENG`	`@0 Evaporative cooling @5 30`
C03	`13`	`X`	`SPA`	`@0 Enfriamiento evaporación @5 30`
N21				`@1 319`

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Le document en format XML

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<author><name sortKey="Ben Jabrallah, S" sort="Ben Jabrallah, S" uniqKey="Ben Jabrallah S" first="S." last="Ben Jabrallah">S. Ben Jabrallah</name>
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<term>Evaporative cooling</term>
<term>Falling film</term>
<term>Finite volume method</term>
<term>Heat mass transfer</term>
<term>Modeling</term>
<term>Numerical simulation</term>
<term>Nusselt number</term>
<term>Vertical cylinder</term>
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</keywords>
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<term>Méthode volume fini</term>
<term>Modélisation</term>
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<term>Transfert chaleur masse</term>
<term>Nombre Nusselt</term>
<term>Cylindre coaxial</term>
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<front><div type="abstract" xml:lang="en">Mixed convection during evaporation of a water falling film in a vertical concentric annulus was studied numerically. The water thin film falls on the inner tube and is subjected to a constant heat flux density, whereas the outer cylinder is assumed to be insulated and dry. An imposed air flow circulates within the gap between the two concentric tubes. The objective of this work is to understand the evaporation phenomenon in order to improve the average evaporated mass flux density and heat and mass transfer. Conservative equations governing the gas phase are solved numerically using the finite volume method. In the liquid phase, a method based on local heat and mass balances on each level is used. Thus, the following liquid film parameters, feed water mass flow, feed temperature and heat flux density, are taken into account. The obtained results are analyzed to emphasize and evaluate the influence of the previous operating parameters and the annulus curvature on the effective evaporation surface and on the mass flux density of evaporated water.</div>
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<fA08 i1="01" i2="1" l="ENG"><s1>Numerical study of evaporation in a vertical annulus heated at the inner wall</s1>
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<fC01 i1="01" l="ENG"><s0>Mixed convection during evaporation of a water falling film in a vertical concentric annulus was studied numerically. The water thin film falls on the inner tube and is subjected to a constant heat flux density, whereas the outer cylinder is assumed to be insulated and dry. An imposed air flow circulates within the gap between the two concentric tubes. The objective of this work is to understand the evaporation phenomenon in order to improve the average evaporated mass flux density and heat and mass transfer. Conservative equations governing the gas phase are solved numerically using the finite volume method. In the liquid phase, a method based on local heat and mass balances on each level is used. Thus, the following liquid film parameters, feed water mass flow, feed temperature and heat flux density, are taken into account. The obtained results are analyzed to emphasize and evaluate the influence of the previous operating parameters and the annulus curvature on the effective evaporation surface and on the mass flux density of evaporated water.</s0>
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</fC02>
<fC02 i1="02" i2="X"><s0>230</s0>
</fC02>
<fC03 i1="01" i2="X" l="FRE"><s0>Convection mixte</s0>
<s5>02</s5>
</fC03>
<fC03 i1="01" i2="X" l="ENG"><s0>Combined convection</s0>
<s5>02</s5>
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<fC03 i1="01" i2="X" l="SPA"><s0>Convección mixta</s0>
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<s5>06</s5>
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<s5>06</s5>
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<s5>06</s5>
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<s5>08</s5>
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<s5>08</s5>
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<s5>08</s5>
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<s5>09</s5>
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<s5>09</s5>
</fC03>
<fC03 i1="04" i2="X" l="SPA"><s0>Cilindro vertical</s0>
<s5>09</s5>
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<s5>10</s5>
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<s5>10</s5>
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<s5>10</s5>
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<s5>12</s5>
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<s5>12</s5>
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<s5>12</s5>
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<s5>15</s5>
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<s5>15</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Modelización</s0>
<s5>15</s5>
</fC03>
<fC03 i1="08" i2="X" l="FRE"><s0>Simulation numérique</s0>
<s5>16</s5>
</fC03>
<fC03 i1="08" i2="X" l="ENG"><s0>Numerical simulation</s0>
<s5>16</s5>
</fC03>
<fC03 i1="08" i2="X" l="SPA"><s0>Simulación numérica</s0>
<s5>16</s5>
</fC03>
<fC03 i1="09" i2="X" l="FRE"><s0>Evaporation</s0>
<s5>23</s5>
</fC03>
<fC03 i1="09" i2="X" l="ENG"><s0>Evaporation</s0>
<s5>23</s5>
</fC03>
<fC03 i1="09" i2="X" l="SPA"><s0>Evaporación</s0>
<s5>23</s5>
</fC03>
<fC03 i1="10" i2="X" l="FRE"><s0>Transfert chaleur masse</s0>
<s5>24</s5>
</fC03>
<fC03 i1="10" i2="X" l="ENG"><s0>Heat mass transfer</s0>
<s5>24</s5>
</fC03>
<fC03 i1="10" i2="X" l="SPA"><s0>Transferencia calor masa</s0>
<s5>24</s5>
</fC03>
<fC03 i1="11" i2="X" l="FRE"><s0>Nombre Nusselt</s0>
<s5>25</s5>
</fC03>
<fC03 i1="11" i2="X" l="ENG"><s0>Nusselt number</s0>
<s5>25</s5>
</fC03>
<fC03 i1="11" i2="X" l="SPA"><s0>Número Nusselt</s0>
<s5>25</s5>
</fC03>
<fC03 i1="12" i2="X" l="FRE"><s0>Cylindre coaxial</s0>
<s5>29</s5>
</fC03>
<fC03 i1="12" i2="X" l="ENG"><s0>Coaxial cylinders</s0>
<s5>29</s5>
</fC03>
<fC03 i1="12" i2="X" l="SPA"><s0>Cilindro coaxial</s0>
<s5>29</s5>
</fC03>
<fC03 i1="13" i2="X" l="FRE"><s0>Refroidissement évaporation</s0>
<s5>30</s5>
</fC03>
<fC03 i1="13" i2="X" l="ENG"><s0>Evaporative cooling</s0>
<s5>30</s5>
</fC03>
<fC03 i1="13" i2="X" l="SPA"><s0>Enfriamiento evaporación</s0>
<s5>30</s5>
</fC03>
<fN21><s1>319</s1>
</fN21>
</pA>
</standard>
</inist>
</record>

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Numerical study of evaporation in a vertical annulus heated at the inner wall

Numerical study of evaporation in a vertical annulus heated at the inner wall

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