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FLUX ENHANCEMENT DURING ULTRAFILTRATION OF DEPECTINIZED MOSAMBI (CITRUS SINENSIS [L] OSBECK) JUICE

Identifieur interne : 000232 ( PascalFrancis/Corpus ); précédent : 000231; suivant : 000233

FLUX ENHANCEMENT DURING ULTRAFILTRATION OF DEPECTINIZED MOSAMBI (CITRUS SINENSIS [L] OSBECK) JUICE

Auteurs : P. Rai ; G. C. Majumdar ; S. Dasgupta ; S. De

Source :

RBID : Pascal:10-0341456

Descripteurs français

English descriptors

Abstract

The effect of alteration in hydrodynamic conditions and external electric field on the permeate flux during ultrafiltration of synthetic and mosambi juice in a cross flow channel has been studied. The hydrodynamic conditions inside the cross flow channel were altered by imposing laminar flow, laminar flow with turbulent promoters, flow in the transition (in case of synthetic juice) and turbulent (in case of actual juice) regime. The steady state permeate flux was in the range of 17.5 to 18.5 L/m2h (at Re = 657, laminar flow) for operating pressures (276 to 552 kPa). This range was in between 18 and 22.5 L/m2h using turbulent promoters at the same Reynolds number and in between 35 and 43 L/m2h in the transition flow regime at the same operating pressure. In the third case, the effects of external electric field (a body force) on the flux enhancement were explored. The steady state flux of the synthetic juice increased by about 20% when the external electric field was applied gradually up to 1,600 v/m. For actual depectinized mosambi juice, about 50% enhancement of steady state flux was achieved with an external electric field of strength 500 v/m.

Notice en format standard (ISO 2709)

Pour connaître la documentation sur le format Inist Standard.

pA  
A01 01  1    @0 0145-8876
A02 01      @0 JFPEDM
A03   1    @0 J. food process eng.
A05       @2 33
A06       @2 3
A08 01  1  ENG  @1 FLUX ENHANCEMENT DURING ULTRAFILTRATION OF DEPECTINIZED MOSAMBI (CITRUS SINENSIS [L] OSBECK) JUICE
A11 01  1    @1 RAI (P.)
A11 02  1    @1 MAJUMDAR (G. C.)
A11 03  1    @1 DASGUPTA (S.)
A11 04  1    @1 DE (S.)
A14 01      @1 Department of Agricultural Engineering Birsa Agricultural University Kanke @2 Ranchi @3 IND @Z 1 aut.
A14 02      @1 Department of Agriculture and Food Engineering Indian Institute of Technology, Kharagpur @2 Kharagpur- 721 302 @3 IND @Z 2 aut.
A14 03      @1 Department of Chemical Engineering Indian Institute of Technology, Kharagpur @2 Kharagpur- 721 302 @3 IND @Z 3 aut. @Z 4 aut.
A20       @1 554-567
A21       @1 2010
A23 01      @0 ENG
A43 01      @1 INIST @2 17763 @5 354000181783850110
A44       @0 0000 @1 © 2010 INIST-CNRS. All rights reserved.
A45       @0 1/2 p.
A47 01  1    @0 10-0341456
A60       @1 P
A61       @0 A
A64 01  1    @0 Journal of food process engineering
A66 01      @0 USA
C01 01    ENG  @0 The effect of alteration in hydrodynamic conditions and external electric field on the permeate flux during ultrafiltration of synthetic and mosambi juice in a cross flow channel has been studied. The hydrodynamic conditions inside the cross flow channel were altered by imposing laminar flow, laminar flow with turbulent promoters, flow in the transition (in case of synthetic juice) and turbulent (in case of actual juice) regime. The steady state permeate flux was in the range of 17.5 to 18.5 L/m2h (at Re = 657, laminar flow) for operating pressures (276 to 552 kPa). This range was in between 18 and 22.5 L/m2h using turbulent promoters at the same Reynolds number and in between 35 and 43 L/m2h in the transition flow regime at the same operating pressure. In the third case, the effects of external electric field (a body force) on the flux enhancement were explored. The steady state flux of the synthetic juice increased by about 20% when the external electric field was applied gradually up to 1,600 v/m. For actual depectinized mosambi juice, about 50% enhancement of steady state flux was achieved with an external electric field of strength 500 v/m.
C02 01  X    @0 002A35
C03 01  X  FRE  @0 Flux @5 01
C03 01  X  ENG  @0 Flux @5 01
C03 01  X  SPA  @0 Flujo @5 01
C03 02  X  FRE  @0 Ultrafiltration @5 02
C03 02  X  ENG  @0 Ultrafiltration @5 02
C03 02  X  SPA  @0 Ultrafiltración @5 02
C03 03  X  FRE  @0 Citrus sinensis @2 NS @5 10
C03 03  X  ENG  @0 Citrus sinensis @2 NS @5 10
C03 03  X  SPA  @0 Citrus sinensis @2 NS @5 10
C07 01  X  FRE  @0 Rutaceae @2 NS
C07 01  X  ENG  @0 Rutaceae @2 NS
C07 01  X  SPA  @0 Rutaceae @2 NS
C07 02  X  FRE  @0 Dicotyledones @2 NS
C07 02  X  ENG  @0 Dicotyledones @2 NS
C07 02  X  SPA  @0 Dicotyledones @2 NS
C07 03  X  FRE  @0 Angiospermae @2 NS
C07 03  X  ENG  @0 Angiospermae @2 NS
C07 03  X  SPA  @0 Angiospermae @2 NS
C07 04  X  FRE  @0 Spermatophyta @2 NS
C07 04  X  ENG  @0 Spermatophyta @2 NS
C07 04  X  SPA  @0 Spermatophyta @2 NS
N21       @1 221
N44 01      @1 OTO
N82       @1 OTO

Format Inist (serveur)

NO : PASCAL 10-0341456 INIST
ET : FLUX ENHANCEMENT DURING ULTRAFILTRATION OF DEPECTINIZED MOSAMBI (CITRUS SINENSIS [L] OSBECK) JUICE
AU : RAI (P.); MAJUMDAR (G. C.); DASGUPTA (S.); DE (S.)
AF : Department of Agricultural Engineering Birsa Agricultural University Kanke/Ranchi/Inde (1 aut.); Department of Agriculture and Food Engineering Indian Institute of Technology, Kharagpur/Kharagpur- 721 302/Inde (2 aut.); Department of Chemical Engineering Indian Institute of Technology, Kharagpur/Kharagpur- 721 302/Inde (3 aut., 4 aut.)
DT : Publication en série; Niveau analytique
SO : Journal of food process engineering; ISSN 0145-8876; Coden JFPEDM; Etats-Unis; Da. 2010; Vol. 33; No. 3; Pp. 554-567; Bibl. 1/2 p.
LA : Anglais
EA : The effect of alteration in hydrodynamic conditions and external electric field on the permeate flux during ultrafiltration of synthetic and mosambi juice in a cross flow channel has been studied. The hydrodynamic conditions inside the cross flow channel were altered by imposing laminar flow, laminar flow with turbulent promoters, flow in the transition (in case of synthetic juice) and turbulent (in case of actual juice) regime. The steady state permeate flux was in the range of 17.5 to 18.5 L/m2h (at Re = 657, laminar flow) for operating pressures (276 to 552 kPa). This range was in between 18 and 22.5 L/m2h using turbulent promoters at the same Reynolds number and in between 35 and 43 L/m2h in the transition flow regime at the same operating pressure. In the third case, the effects of external electric field (a body force) on the flux enhancement were explored. The steady state flux of the synthetic juice increased by about 20% when the external electric field was applied gradually up to 1,600 v/m. For actual depectinized mosambi juice, about 50% enhancement of steady state flux was achieved with an external electric field of strength 500 v/m.
CC : 002A35
FD : Flux; Ultrafiltration; Citrus sinensis
FG : Rutaceae; Dicotyledones; Angiospermae; Spermatophyta
ED : Flux; Ultrafiltration; Citrus sinensis
EG : Rutaceae; Dicotyledones; Angiospermae; Spermatophyta
SD : Flujo; Ultrafiltración; Citrus sinensis
LO : INIST-17763.354000181783850110
ID : 10-0341456

Links to Exploration step

Pascal:10-0341456

Le document en format XML

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<div type="abstract" xml:lang="en">The effect of alteration in hydrodynamic conditions and external electric field on the permeate flux during ultrafiltration of synthetic and mosambi juice in a cross flow channel has been studied. The hydrodynamic conditions inside the cross flow channel were altered by imposing laminar flow, laminar flow with turbulent promoters, flow in the transition (in case of synthetic juice) and turbulent (in case of actual juice) regime. The steady state permeate flux was in the range of 17.5 to 18.5 L/m
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h in the transition flow regime at the same operating pressure. In the third case, the effects of external electric field (a body force) on the flux enhancement were explored. The steady state flux of the synthetic juice increased by about 20% when the external electric field was applied gradually up to 1,600 v/m. For actual depectinized mosambi juice, about 50% enhancement of steady state flux was achieved with an external electric field of strength 500 v/m.</div>
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h in the transition flow regime at the same operating pressure. In the third case, the effects of external electric field (a body force) on the flux enhancement were explored. The steady state flux of the synthetic juice increased by about 20% when the external electric field was applied gradually up to 1,600 v/m. For actual depectinized mosambi juice, about 50% enhancement of steady state flux was achieved with an external electric field of strength 500 v/m.</s0>
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<ET>FLUX ENHANCEMENT DURING ULTRAFILTRATION OF DEPECTINIZED MOSAMBI (CITRUS SINENSIS [L] OSBECK) JUICE</ET>
<AU>RAI (P.); MAJUMDAR (G. C.); DASGUPTA (S.); DE (S.)</AU>
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<sup>2</sup>
h (at Re = 657, laminar flow) for operating pressures (276 to 552 kPa). This range was in between 18 and 22.5 L/m
<sup>2</sup>
h using turbulent promoters at the same Reynolds number and in between 35 and 43 L/m
<sup>2</sup>
h in the transition flow regime at the same operating pressure. In the third case, the effects of external electric field (a body force) on the flux enhancement were explored. The steady state flux of the synthetic juice increased by about 20% when the external electric field was applied gradually up to 1,600 v/m. For actual depectinized mosambi juice, about 50% enhancement of steady state flux was achieved with an external electric field of strength 500 v/m.</EA>
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