AustralieFrV1, PascalFrancis, Corpus, bibRecord, 001055

Effects of Sludge Concentrations and Different Sponge Configurations on the Performance of a Sponge-Submerged Membrane Bioreactor

Identifieur interne : 001055 ( PascalFrancis/Corpus ); précédent : 001054; suivant : 001056

Effects of Sludge Concentrations and Different Sponge Configurations on the Performance of a Sponge-Submerged Membrane Bioreactor

Auteurs : Tien Thanh Nguyen ; HUU HAO NGO ; WENSHAN GUO ; JIANXIN LI ; Andrzej Listowski

Source :

Applied biochemistry and biotechnology [ 0273-2289 ] ; 2012.

RBID : Pascal:12-0357674

Descripteurs français

Pascal (Inist)
- Boue activée, Concentration, Porifera, Bioréacteur, Réacteur membrane, Membrane, Encrassement, Nutriment.

English descriptors

KwdEn :
- Activated sludge, Bioreactor, Concentration, Fouling, Membrane, Membrane reactor, Nutrient, Porifera.

Abstract

The performance of a novel sponge-submerged membrane bioreactor (SSMBR) was evaluated to treat primary treated sewage effluent at three different activated sludge concentrations. Polyurethane sponge cubes with size of 1 × 1 × 1 cm were used as attached growth media in the bioreactor. The results indicated the successful removal of organic carbon and phosphorous with the efficiency higher than 98% at all conditions. Acclimatised sponge MBR showed about 5% better ammonia nitrogen removal at 5 and 10 g/L sludge concentration as compared to the new sponge system. The respiration test revealed that the specific oxygen uptake rate was around 1.0-3.5 mgO₂/gVSS.h and likely more stable at 10 g/L sludge concentration. The sludge volume index of less than 100 mL/g during the operation indicated the good settling property of the sludge. The low mixed liquor suspended solid increase indicated that SSMBR could control the sludge production. This SSMBR was also successful in reducing membrane fouling with significant lower transmembrane pressure (e.g. only 0.5 kPa/day) compared to the conventional MBR system. Further study will be conducted to optimise other operating conditions.

Notice en format standard (ISO 2709)

Pour connaître la documentation sur le format Inist Standard.

A01	`01`	`1`		`@0 0273-2289`
A02	`01`			`@0 ABIBDL`
A03		`1`		`@0 Appl. biochem. biotechnol.`
A05				`@2 167`
A06				`@2 6`
A08	`01`	`1`	`ENG`	`@1 Effects of Sludge Concentrations and Different Sponge Configurations on the Performance of a Sponge-Submerged Membrane Bioreactor`
A09	`01`	`1`	`ENG`	`@1 New Horizons in Biotechnology`
A11	`01`	`1`		`@1 NGUYEN (Tien Thanh)`
A11	`02`	`1`		`@1 HUU HAO NGO`
A11	`03`	`1`		`@1 WENSHAN GUO`
A11	`04`	`1`		`@1 JIANXIN LI`
A11	`05`	`1`		`@1 LISTOWSKI (Andrzej)`
A12	`01`	`1`		`@1 PANDEY (Ashok) @9 ed.`
A12	`02`	`1`		`@1 LARROCHE (Christian) @9 ed.`
A12	`03`	`1`		`@1 LEE (Duu-Jong) @9 ed.`
A12	`04`	`1`		`@1 SOCCOL (Carlos Ricardo) @9 ed.`
A14	`01`			`@1 Centre for Technology in Water and Wastewater, School of Civil and Environmental Engineering, University of Technology Sydney @2 Broadway, NSW 2007 @3 AUS @Z 1 aut. @Z 2 aut. @Z 3 aut.`
A14	`02`			`@1 Laboratory for Membrane Materials and Separation Technology, Shanghai Advanced Research Institute, Chinese Academy of Sciences @2 Shanghai 201203 @3 CHN @Z 4 aut.`
A14	`03`			`@1 State Key Laboratory of Hollow Fiber Membrane Materials and Processes, School of Materials Science and Engineering, Tianjin Polytechnic University @2 Tianjin 300160 @3 CHN @Z 4 aut.`
A14	`04`			`@1 Sydney Olympic Park Authority @2 Sydney Olympic Park, NSW 2127 @3 AUS @Z 5 aut.`
A15	`01`			`@1 Centre for Biofuels, National Institute for Interdisciplinary Science and Technology, CSIR @2 Trivandrum 695 019 @3 IND @Z 1 aut.`
A15	`02`			`@1 Université Blaise Pascal Laboratoire de Génie Chimique et Biochimique, Polytech Clermont-Ferrand, Clermont University, 24 av. des Landais, BP 206 @2 63174 Aubière @3 FRA @Z 2 aut.`
A15	`03`			`@1 Department of Chemical Engineering, National Taiwan University of Science and Technology @2 Taipei 10617 @3 TWN @Z 3 aut.`
A20				`@1 1678-1687`
A21				`@1 2012`
A23	`01`			`@0 ENG`
A43	`01`			`@1 INIST @2 17423 @5 354000508326590180`
A44				`@0 0000 @1 © 2012 INIST-CNRS. All rights reserved.`
A45				`@0 24 ref.`
A47	`01`	`1`		`@0 12-0357674`
A60				`@1 P`
A61				`@0 A`
A64	`01`	`1`		`@0 Applied biochemistry and biotechnology`
A66	`01`			`@0 DEU`
C01	`01`		`ENG`	@0 The performance of a novel sponge-submerged membrane bioreactor (SSMBR) was evaluated to treat primary treated sewage effluent at three different activated sludge concentrations. Polyurethane sponge cubes with size of 1 × 1 × 1 cm were used as attached growth media in the bioreactor. The results indicated the successful removal of organic carbon and phosphorous with the efficiency higher than 98% at all conditions. Acclimatised sponge MBR showed about 5% better ammonia nitrogen removal at 5 and 10 g/L sludge concentration as compared to the new sponge system. The respiration test revealed that the specific oxygen uptake rate was around 1.0-3.5 mgO₂/gVSS.h and likely more stable at 10 g/L sludge concentration. The sludge volume index of less than 100 mL/g during the operation indicated the good settling property of the sludge. The low mixed liquor suspended solid increase indicated that SSMBR could control the sludge production. This SSMBR was also successful in reducing membrane fouling with significant lower transmembrane pressure (e.g. only 0.5 kPa/day) compared to the conventional MBR system. Further study will be conducted to optimise other operating conditions.
C02	`01`	`X`		`@0 002A31C09A`
C02	`02`	`X`		`@0 215`
C03	`01`	`X`	`FRE`	`@0 Boue activée @5 01`
C03	`01`	`X`	`ENG`	`@0 Activated sludge @5 01`
C03	`01`	`X`	`SPA`	`@0 Lodo activado @5 01`
C03	`02`	`X`	`FRE`	`@0 Concentration @5 02`
C03	`02`	`X`	`ENG`	`@0 Concentration @5 02`
C03	`02`	`X`	`SPA`	`@0 Concentración @5 02`
C03	`03`	`X`	`FRE`	`@0 Porifera @2 NS @5 10`
C03	`03`	`X`	`ENG`	`@0 Porifera @2 NS @5 10`
C03	`03`	`X`	`SPA`	`@0 Porifera @2 NS @5 10`
C03	`04`	`X`	`FRE`	`@0 Bioréacteur @5 11`
C03	`04`	`X`	`ENG`	`@0 Bioreactor @5 11`
C03	`04`	`X`	`SPA`	`@0 Biorreactor @5 11`
C03	`05`	`X`	`FRE`	`@0 Réacteur membrane @5 12`
C03	`05`	`X`	`ENG`	`@0 Membrane reactor @5 12`
C03	`05`	`X`	`SPA`	`@0 Reactor membrana @5 12`
C03	`06`	`X`	`FRE`	`@0 Membrane @5 19`
C03	`06`	`X`	`ENG`	`@0 Membrane @5 19`
C03	`06`	`X`	`SPA`	`@0 Membrana @5 19`
C03	`07`	`X`	`FRE`	`@0 Encrassement @5 20`
C03	`07`	`X`	`ENG`	`@0 Fouling @5 20`
C03	`07`	`X`	`SPA`	`@0 Enmugrecimiento @5 20`
C03	`08`	`X`	`FRE`	`@0 Nutriment @5 21`
C03	`08`	`X`	`ENG`	`@0 Nutrient @5 21`
C03	`08`	`X`	`SPA`	`@0 Nutriente @5 21`
C07	`01`	`X`	`FRE`	`@0 Invertebrata @2 NS`
C07	`01`	`X`	`ENG`	`@0 Invertebrata @2 NS`
C07	`01`	`X`	`SPA`	`@0 Invertebrata @2 NS`
N21				`@1 275`
N44	`01`			`@1 OTO`
N82				`@1 OTO`

Format Inist (serveur)

NO :	PASCAL 12-0357674 INIST
ET :	Effects of Sludge Concentrations and Different Sponge Configurations on the Performance of a Sponge-Submerged Membrane Bioreactor
AU :	NGUYEN (Tien Thanh); HUU HAO NGO; WENSHAN GUO; JIANXIN LI; LISTOWSKI (Andrzej); PANDEY (Ashok); LARROCHE (Christian); LEE (Duu-Jong); SOCCOL (Carlos Ricardo)
AF :	Centre for Technology in Water and Wastewater, School of Civil and Environmental Engineering, University of Technology Sydney/Broadway, NSW 2007/Australie (1 aut., 2 aut., 3 aut.); Laboratory for Membrane Materials and Separation Technology, Shanghai Advanced Research Institute, Chinese Academy of Sciences/Shanghai 201203/Chine (4 aut.); State Key Laboratory of Hollow Fiber Membrane Materials and Processes, School of Materials Science and Engineering, Tianjin Polytechnic University/Tianjin 300160/Chine (4 aut.); Sydney Olympic Park Authority/Sydney Olympic Park, NSW 2127/Australie (5 aut.); Centre for Biofuels, National Institute for Interdisciplinary Science and Technology, CSIR/Trivandrum 695 019/Inde (1 aut.); Université Blaise Pascal Laboratoire de Génie Chimique et Biochimique, Polytech Clermont-Ferrand, Clermont University, 24 av. des Landais, BP 206/63174 Aubière/France (2 aut.); Department of Chemical Engineering, National Taiwan University of Science and Technology/Taipei 10617/Taïwan (3 aut.)
DT :	Publication en série; Niveau analytique
SO :	Applied biochemistry and biotechnology; ISSN 0273-2289; Coden ABIBDL; Allemagne; Da. 2012; Vol. 167; No. 6; Pp. 1678-1687; Bibl. 24 ref.
LA :	Anglais
EA :	The performance of a novel sponge-submerged membrane bioreactor (SSMBR) was evaluated to treat primary treated sewage effluent at three different activated sludge concentrations. Polyurethane sponge cubes with size of 1 × 1 × 1 cm were used as attached growth media in the bioreactor. The results indicated the successful removal of organic carbon and phosphorous with the efficiency higher than 98% at all conditions. Acclimatised sponge MBR showed about 5% better ammonia nitrogen removal at 5 and 10 g/L sludge concentration as compared to the new sponge system. The respiration test revealed that the specific oxygen uptake rate was around 1.0-3.5 mgO₂/gVSS.h and likely more stable at 10 g/L sludge concentration. The sludge volume index of less than 100 mL/g during the operation indicated the good settling property of the sludge. The low mixed liquor suspended solid increase indicated that SSMBR could control the sludge production. This SSMBR was also successful in reducing membrane fouling with significant lower transmembrane pressure (e.g. only 0.5 kPa/day) compared to the conventional MBR system. Further study will be conducted to optimise other operating conditions.
CC :	002A31C09A; 215
FD :	Boue activée; Concentration; Porifera; Bioréacteur; Réacteur membrane; Membrane; Encrassement; Nutriment
FG :	Invertebrata
ED :	Activated sludge; Concentration; Porifera; Bioreactor; Membrane reactor; Membrane; Fouling; Nutrient
EG :	Invertebrata
SD :	Lodo activado; Concentración; Porifera; Biorreactor; Reactor membrana; Membrana; Enmugrecimiento; Nutriente
LO :	INIST-17423.354000508326590180
ID :	12-0357674

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Pascal:12-0357674

Le document en format XML

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<front><div type="abstract" xml:lang="en">The performance of a novel sponge-submerged membrane bioreactor (SSMBR) was evaluated to treat primary treated sewage effluent at three different activated sludge concentrations. Polyurethane sponge cubes with size of 1 × 1 × 1 cm were used as attached growth media in the bioreactor. The results indicated the successful removal of organic carbon and phosphorous with the efficiency higher than 98% at all conditions. Acclimatised sponge MBR showed about 5% better ammonia nitrogen removal at 5 and 10 g/L sludge concentration as compared to the new sponge system. The respiration test revealed that the specific oxygen uptake rate was around 1.0-3.5 mgO<sub>2</sub>
/gVSS.h and likely more stable at 10 g/L sludge concentration. The sludge volume index of less than 100 mL/g during the operation indicated the good settling property of the sludge. The low mixed liquor suspended solid increase indicated that SSMBR could control the sludge production. This SSMBR was also successful in reducing membrane fouling with significant lower transmembrane pressure (e.g. only 0.5 kPa/day) compared to the conventional MBR system. Further study will be conducted to optimise other operating conditions.</div>
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<s3>FRA</s3>
<sZ>2 aut.</sZ>
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<fC01 i1="01" l="ENG"><s0>The performance of a novel sponge-submerged membrane bioreactor (SSMBR) was evaluated to treat primary treated sewage effluent at three different activated sludge concentrations. Polyurethane sponge cubes with size of 1 × 1 × 1 cm were used as attached growth media in the bioreactor. The results indicated the successful removal of organic carbon and phosphorous with the efficiency higher than 98% at all conditions. Acclimatised sponge MBR showed about 5% better ammonia nitrogen removal at 5 and 10 g/L sludge concentration as compared to the new sponge system. The respiration test revealed that the specific oxygen uptake rate was around 1.0-3.5 mgO<sub>2</sub>
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<s5>01</s5>
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<fC03 i1="01" i2="X" l="ENG"><s0>Activated sludge</s0>
<s5>01</s5>
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<s5>01</s5>
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<s5>02</s5>
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<fC03 i1="02" i2="X" l="ENG"><s0>Concentration</s0>
<s5>02</s5>
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<fC03 i1="02" i2="X" l="SPA"><s0>Concentración</s0>
<s5>02</s5>
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<fC03 i1="03" i2="X" l="FRE"><s0>Porifera</s0>
<s2>NS</s2>
<s5>10</s5>
</fC03>
<fC03 i1="03" i2="X" l="ENG"><s0>Porifera</s0>
<s2>NS</s2>
<s5>10</s5>
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<fC03 i1="03" i2="X" l="SPA"><s0>Porifera</s0>
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<s5>10</s5>
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<s5>11</s5>
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<s5>11</s5>
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<fC03 i1="04" i2="X" l="SPA"><s0>Biorreactor</s0>
<s5>11</s5>
</fC03>
<fC03 i1="05" i2="X" l="FRE"><s0>Réacteur membrane</s0>
<s5>12</s5>
</fC03>
<fC03 i1="05" i2="X" l="ENG"><s0>Membrane reactor</s0>
<s5>12</s5>
</fC03>
<fC03 i1="05" i2="X" l="SPA"><s0>Reactor membrana</s0>
<s5>12</s5>
</fC03>
<fC03 i1="06" i2="X" l="FRE"><s0>Membrane</s0>
<s5>19</s5>
</fC03>
<fC03 i1="06" i2="X" l="ENG"><s0>Membrane</s0>
<s5>19</s5>
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<fC03 i1="06" i2="X" l="SPA"><s0>Membrana</s0>
<s5>19</s5>
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<fC03 i1="07" i2="X" l="FRE"><s0>Encrassement</s0>
<s5>20</s5>
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<fC03 i1="07" i2="X" l="ENG"><s0>Fouling</s0>
<s5>20</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Enmugrecimiento</s0>
<s5>20</s5>
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<fC03 i1="08" i2="X" l="FRE"><s0>Nutriment</s0>
<s5>21</s5>
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<s5>21</s5>
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<s5>21</s5>
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<s2>NS</s2>
</fC07>
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<s2>NS</s2>
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<fC07 i1="01" i2="X" l="SPA"><s0>Invertebrata</s0>
<s2>NS</s2>
</fC07>
<fN21><s1>275</s1>
</fN21>
<fN44 i1="01"><s1>OTO</s1>
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<server><NO>PASCAL 12-0357674 INIST</NO>
<ET>Effects of Sludge Concentrations and Different Sponge Configurations on the Performance of a Sponge-Submerged Membrane Bioreactor</ET>
<AU>NGUYEN (Tien Thanh); HUU HAO NGO; WENSHAN GUO; JIANXIN LI; LISTOWSKI (Andrzej); PANDEY (Ashok); LARROCHE (Christian); LEE (Duu-Jong); SOCCOL (Carlos Ricardo)</AU>
<AF>Centre for Technology in Water and Wastewater, School of Civil and Environmental Engineering, University of Technology Sydney/Broadway, NSW 2007/Australie (1 aut., 2 aut., 3 aut.); Laboratory for Membrane Materials and Separation Technology, Shanghai Advanced Research Institute, Chinese Academy of Sciences/Shanghai 201203/Chine (4 aut.); State Key Laboratory of Hollow Fiber Membrane Materials and Processes, School of Materials Science and Engineering, Tianjin Polytechnic University/Tianjin 300160/Chine (4 aut.); Sydney Olympic Park Authority/Sydney Olympic Park, NSW 2127/Australie (5 aut.); Centre for Biofuels, National Institute for Interdisciplinary Science and Technology, CSIR/Trivandrum 695 019/Inde (1 aut.); Université Blaise Pascal Laboratoire de Génie Chimique et Biochimique, Polytech Clermont-Ferrand, Clermont University, 24 av. des Landais, BP 206/63174 Aubière/France (2 aut.); Department of Chemical Engineering, National Taiwan University of Science and Technology/Taipei 10617/Taïwan (3 aut.)</AF>
<DT>Publication en série; Niveau analytique</DT>
<SO>Applied biochemistry and biotechnology; ISSN 0273-2289; Coden ABIBDL; Allemagne; Da. 2012; Vol. 167; No. 6; Pp. 1678-1687; Bibl. 24 ref.</SO>
<LA>Anglais</LA>
<EA>The performance of a novel sponge-submerged membrane bioreactor (SSMBR) was evaluated to treat primary treated sewage effluent at three different activated sludge concentrations. Polyurethane sponge cubes with size of 1 × 1 × 1 cm were used as attached growth media in the bioreactor. The results indicated the successful removal of organic carbon and phosphorous with the efficiency higher than 98% at all conditions. Acclimatised sponge MBR showed about 5% better ammonia nitrogen removal at 5 and 10 g/L sludge concentration as compared to the new sponge system. The respiration test revealed that the specific oxygen uptake rate was around 1.0-3.5 mgO<sub>2</sub>
/gVSS.h and likely more stable at 10 g/L sludge concentration. The sludge volume index of less than 100 mL/g during the operation indicated the good settling property of the sludge. The low mixed liquor suspended solid increase indicated that SSMBR could control the sludge production. This SSMBR was also successful in reducing membrane fouling with significant lower transmembrane pressure (e.g. only 0.5 kPa/day) compared to the conventional MBR system. Further study will be conducted to optimise other operating conditions.</EA>
<CC>002A31C09A; 215</CC>
<FD>Boue activée; Concentration; Porifera; Bioréacteur; Réacteur membrane; Membrane; Encrassement; Nutriment</FD>
<FG>Invertebrata</FG>
<ED>Activated sludge; Concentration; Porifera; Bioreactor; Membrane reactor; Membrane; Fouling; Nutrient</ED>
<EG>Invertebrata</EG>
<SD>Lodo activado; Concentración; Porifera; Biorreactor; Reactor membrana; Membrana; Enmugrecimiento; Nutriente</SD>
<LO>INIST-17423.354000508326590180</LO>
<ID>12-0357674</ID>
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Effects of Sludge Concentrations and Different Sponge Configurations on the Performance of a Sponge-Submerged Membrane Bioreactor

Effects of Sludge Concentrations and Different Sponge Configurations on the Performance of a Sponge-Submerged Membrane Bioreactor

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