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Evaluation of succinic acid continuous and repeat-batch biofilm fermentation by Actinobacillus succinogenes using plastic composite support bioreactors
Continuous and repeat-batch biofilm fermentations using Actinobacillus succinogenes were performed with immobilized and suspended-cell systems. For the immobilized continuous system, plastic composite supports (PCS) containing 50% (w/w) polypropylene (PP), 35% (w/w) ground soybean hulls, 5% (w/w) dr...
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Published in: | Applied microbiology and biotechnology 2004-11, Vol.65 (6), p.664-670 |
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description | Continuous and repeat-batch biofilm fermentations using Actinobacillus succinogenes were performed with immobilized and suspended-cell systems. For the immobilized continuous system, plastic composite supports (PCS) containing 50% (w/w) polypropylene (PP), 35% (w/w) ground soybean hulls, 5% (w/w) dried bovine albumin, 2.5% (w/w) soybean flour, 2.5% (w/w) yeast extract, 2.5% (w/w) dried red blood cells, and 2.5% (w/w) peptone, or PP tubes (8.5 cm in length) were arranged around the agitator shaft in a grid formation. Agitation was controlled at 125 rpm and 150 rpm. Samples were taken at dilution rates of 0.2, 0.4, 0.6, 0.8, 1.0, and 1.2 h(-1) and analyzed for succinic acid production and glucose consumption (g l(-1)). For PCS bioreactors, the highest final succinic acid concentrations (10.1 g(-1), 10.4 g l(-1)) and percentage yields (62.6%, 71.6%) occurred at the dilution rate of 0.2 h(-1). PCS disks were evaluated in a repeat-batch biofilm reactor. Suspended-cell batch fermentations were performed in flasks and a repeat-batch bioreactor. The maximum concentration of succinic acid produced was 40 g l(-1). Peak succinic acid percentage yields in continuous and repeat-batch fermentations of A. succinogenes were observed in suspended-cell continuous fermentations at a dilution rate of 1.0 h(-1) (76.2%) and in PCS repeat-batch fermentations with an initial glucose concentration of 40 g l(-1) (86.7%). |
doi_str_mv | 10.1007/s00253-004-1634-2 |
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III ; DiSpirito, A.A ; Denli, Y</creator><creatorcontrib>Urbance, S.E ; Pometto, A.L. III ; DiSpirito, A.A ; Denli, Y</creatorcontrib><description>Continuous and repeat-batch biofilm fermentations using Actinobacillus succinogenes were performed with immobilized and suspended-cell systems. For the immobilized continuous system, plastic composite supports (PCS) containing 50% (w/w) polypropylene (PP), 35% (w/w) ground soybean hulls, 5% (w/w) dried bovine albumin, 2.5% (w/w) soybean flour, 2.5% (w/w) yeast extract, 2.5% (w/w) dried red blood cells, and 2.5% (w/w) peptone, or PP tubes (8.5 cm in length) were arranged around the agitator shaft in a grid formation. Agitation was controlled at 125 rpm and 150 rpm. Samples were taken at dilution rates of 0.2, 0.4, 0.6, 0.8, 1.0, and 1.2 h(-1) and analyzed for succinic acid production and glucose consumption (g l(-1)). For PCS bioreactors, the highest final succinic acid concentrations (10.1 g(-1), 10.4 g l(-1)) and percentage yields (62.6%, 71.6%) occurred at the dilution rate of 0.2 h(-1). PCS disks were evaluated in a repeat-batch biofilm reactor. Suspended-cell batch fermentations were performed in flasks and a repeat-batch bioreactor. The maximum concentration of succinic acid produced was 40 g l(-1). Peak succinic acid percentage yields in continuous and repeat-batch fermentations of A. succinogenes were observed in suspended-cell continuous fermentations at a dilution rate of 1.0 h(-1) (76.2%) and in PCS repeat-batch fermentations with an initial glucose concentration of 40 g l(-1) (86.7%).</description><identifier>ISSN: 0175-7598</identifier><identifier>EISSN: 1432-0614</identifier><identifier>DOI: 10.1007/s00253-004-1634-2</identifier><identifier>PMID: 15205933</identifier><identifier>CODEN: AMBIDG</identifier><language>eng</language><publisher>Berlin: Springer</publisher><subject>Acid production ; Acids ; Actinobacillus - growth & development ; Actinobacillus - metabolism ; Actinobacillus succinogenes ; Bacteria ; batch fermentation ; Biofilms ; Biofilms - growth & development ; Biological and medical sciences ; Bioreactors ; Biotechnology ; Biotechnology - methods ; Cells, Immobilized ; continuous fermentation ; Culture Media - chemistry ; Fermentation ; Fundamental and applied biological sciences. 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III</creatorcontrib><creatorcontrib>DiSpirito, A.A</creatorcontrib><creatorcontrib>Denli, Y</creatorcontrib><title>Evaluation of succinic acid continuous and repeat-batch biofilm fermentation by Actinobacillus succinogenes using plastic composite support bioreactors</title><title>Applied microbiology and biotechnology</title><addtitle>Appl Microbiol Biotechnol</addtitle><description>Continuous and repeat-batch biofilm fermentations using Actinobacillus succinogenes were performed with immobilized and suspended-cell systems. For the immobilized continuous system, plastic composite supports (PCS) containing 50% (w/w) polypropylene (PP), 35% (w/w) ground soybean hulls, 5% (w/w) dried bovine albumin, 2.5% (w/w) soybean flour, 2.5% (w/w) yeast extract, 2.5% (w/w) dried red blood cells, and 2.5% (w/w) peptone, or PP tubes (8.5 cm in length) were arranged around the agitator shaft in a grid formation. Agitation was controlled at 125 rpm and 150 rpm. Samples were taken at dilution rates of 0.2, 0.4, 0.6, 0.8, 1.0, and 1.2 h(-1) and analyzed for succinic acid production and glucose consumption (g l(-1)). For PCS bioreactors, the highest final succinic acid concentrations (10.1 g(-1), 10.4 g l(-1)) and percentage yields (62.6%, 71.6%) occurred at the dilution rate of 0.2 h(-1). PCS disks were evaluated in a repeat-batch biofilm reactor. Suspended-cell batch fermentations were performed in flasks and a repeat-batch bioreactor. The maximum concentration of succinic acid produced was 40 g l(-1). Peak succinic acid percentage yields in continuous and repeat-batch fermentations of A. succinogenes were observed in suspended-cell continuous fermentations at a dilution rate of 1.0 h(-1) (76.2%) and in PCS repeat-batch fermentations with an initial glucose concentration of 40 g l(-1) (86.7%).</description><subject>Acid production</subject><subject>Acids</subject><subject>Actinobacillus - growth & development</subject><subject>Actinobacillus - metabolism</subject><subject>Actinobacillus succinogenes</subject><subject>Bacteria</subject><subject>batch fermentation</subject><subject>Biofilms</subject><subject>Biofilms - growth & development</subject><subject>Biological and medical sciences</subject><subject>Bioreactors</subject><subject>Biotechnology</subject><subject>Biotechnology - methods</subject><subject>Cells, Immobilized</subject><subject>continuous fermentation</subject><subject>Culture Media - chemistry</subject><subject>Fermentation</subject><subject>Fundamental and applied biological sciences. 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III</au><au>DiSpirito, A.A</au><au>Denli, Y</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Evaluation of succinic acid continuous and repeat-batch biofilm fermentation by Actinobacillus succinogenes using plastic composite support bioreactors</atitle><jtitle>Applied microbiology and biotechnology</jtitle><addtitle>Appl Microbiol Biotechnol</addtitle><date>2004-11-01</date><risdate>2004</risdate><volume>65</volume><issue>6</issue><spage>664</spage><epage>670</epage><pages>664-670</pages><issn>0175-7598</issn><eissn>1432-0614</eissn><coden>AMBIDG</coden><abstract>Continuous and repeat-batch biofilm fermentations using Actinobacillus succinogenes were performed with immobilized and suspended-cell systems. For the immobilized continuous system, plastic composite supports (PCS) containing 50% (w/w) polypropylene (PP), 35% (w/w) ground soybean hulls, 5% (w/w) dried bovine albumin, 2.5% (w/w) soybean flour, 2.5% (w/w) yeast extract, 2.5% (w/w) dried red blood cells, and 2.5% (w/w) peptone, or PP tubes (8.5 cm in length) were arranged around the agitator shaft in a grid formation. Agitation was controlled at 125 rpm and 150 rpm. Samples were taken at dilution rates of 0.2, 0.4, 0.6, 0.8, 1.0, and 1.2 h(-1) and analyzed for succinic acid production and glucose consumption (g l(-1)). For PCS bioreactors, the highest final succinic acid concentrations (10.1 g(-1), 10.4 g l(-1)) and percentage yields (62.6%, 71.6%) occurred at the dilution rate of 0.2 h(-1). PCS disks were evaluated in a repeat-batch biofilm reactor. Suspended-cell batch fermentations were performed in flasks and a repeat-batch bioreactor. The maximum concentration of succinic acid produced was 40 g l(-1). Peak succinic acid percentage yields in continuous and repeat-batch fermentations of A. succinogenes were observed in suspended-cell continuous fermentations at a dilution rate of 1.0 h(-1) (76.2%) and in PCS repeat-batch fermentations with an initial glucose concentration of 40 g l(-1) (86.7%).</abstract><cop>Berlin</cop><pub>Springer</pub><pmid>15205933</pmid><doi>10.1007/s00253-004-1634-2</doi><tpages>7</tpages></addata></record> |
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subjects | Acid production Acids Actinobacillus - growth & development Actinobacillus - metabolism Actinobacillus succinogenes Bacteria batch fermentation Biofilms Biofilms - growth & development Biological and medical sciences Bioreactors Biotechnology Biotechnology - methods Cells, Immobilized continuous fermentation Culture Media - chemistry Fermentation Fundamental and applied biological sciences. Psychology Glucose - metabolism Methods. Procedures. Technologies Microbial engineering. Fermentation and microbial culture technology Microbiology Peptones Plastics Soybeans Succinic Acid - metabolism Yeasts |
title | Evaluation of succinic acid continuous and repeat-batch biofilm fermentation by Actinobacillus succinogenes using plastic composite support bioreactors |
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