A Comparison of Simple Rheological Parameters and Simulation Data for Zymomonas mobilis Fermentation Broths with High Substrate Loading in a 3-L Bioreactor
Traditionally, as much as 80% or more of an ethanol fermentation broth is water that must be removed. This mixture is not only costly to separate but also produces a large aqueous stream that must then be disposed of or recycled. Integrative approaches to water reduction include increasing the bioma...
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description | Traditionally, as much as 80% or more of an ethanol fermentation broth is water that must be removed. This mixture is not only costly to separate but also produces a large aqueous stream that must then be disposed of or recycled. Integrative approaches to water reduction include increasing the biomass concentration during fermentation. In this paper, experimental results are presented for the rheological behavior of high-solids enzymatic cellulose hydrolysis and ethanol fermentation for biomass conversion using Solka Floc as the model feedstock. The experimental determination of the viscosity, shear stress, and shear rate relationships of the 10 to 20% slurry concentrations with constant enzyme concentrations are performed with a variable speed rotational viscometer (2.0 to 200 rpm) at 40 °C. The viscosities of enzymatic suspension observed were in range of 0.0418 to 0.0144, 0.233 to 0.0348, and 0.292 to 0.0447 Pa s for shear rates up to 100 reciprocal seconds at 10, 15, and 20% initial solids (w/v), respectively. Computational fluid dynamics analysis of bioreactor mixing demonstrates the change in bioreactor mixing with increasing biomass concentration. The portion-loading method is shown to be effective for processing high-solids slurries. |
doi_str_mv | 10.1007/s12010-007-8105-z |
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This mixture is not only costly to separate but also produces a large aqueous stream that must then be disposed of or recycled. Integrative approaches to water reduction include increasing the biomass concentration during fermentation. In this paper, experimental results are presented for the rheological behavior of high-solids enzymatic cellulose hydrolysis and ethanol fermentation for biomass conversion using Solka Floc as the model feedstock. The experimental determination of the viscosity, shear stress, and shear rate relationships of the 10 to 20% slurry concentrations with constant enzyme concentrations are performed with a variable speed rotational viscometer (2.0 to 200 rpm) at 40 °C. The viscosities of enzymatic suspension observed were in range of 0.0418 to 0.0144, 0.233 to 0.0348, and 0.292 to 0.0447 Pa s for shear rates up to 100 reciprocal seconds at 10, 15, and 20% initial solids (w/v), respectively. Computational fluid dynamics analysis of bioreactor mixing demonstrates the change in bioreactor mixing with increasing biomass concentration. The portion-loading method is shown to be effective for processing high-solids slurries.</description><identifier>ISSN: 0273-2289</identifier><identifier>EISSN: 1559-0291</identifier><identifier>DOI: 10.1007/s12010-007-8105-z</identifier><identifier>PMID: 18425609</identifier><identifier>CODEN: ABIBDL</identifier><language>eng</language><publisher>New York: Humana Press Inc</publisher><subject>Agricultural biotechnology ; Aqueous solutions ; Biochemistry ; Biological and medical sciences ; Biomass ; Bioreactors ; Bioreactors - microbiology ; Biotechnology ; Cell Culture Techniques - methods ; Cellulose ; Chemistry ; Chemistry and Materials Science ; Computer Simulation ; Culture Media - chemistry ; Ethanol ; Fermentation ; Fluid dynamics ; Fundamental and applied biological sciences. Psychology ; Hydrodynamics ; Methods. Procedures. 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This mixture is not only costly to separate but also produces a large aqueous stream that must then be disposed of or recycled. Integrative approaches to water reduction include increasing the biomass concentration during fermentation. In this paper, experimental results are presented for the rheological behavior of high-solids enzymatic cellulose hydrolysis and ethanol fermentation for biomass conversion using Solka Floc as the model feedstock. The experimental determination of the viscosity, shear stress, and shear rate relationships of the 10 to 20% slurry concentrations with constant enzyme concentrations are performed with a variable speed rotational viscometer (2.0 to 200 rpm) at 40 °C. The viscosities of enzymatic suspension observed were in range of 0.0418 to 0.0144, 0.233 to 0.0348, and 0.292 to 0.0447 Pa s for shear rates up to 100 reciprocal seconds at 10, 15, and 20% initial solids (w/v), respectively. Computational fluid dynamics analysis of bioreactor mixing demonstrates the change in bioreactor mixing with increasing biomass concentration. The portion-loading method is shown to be effective for processing high-solids slurries.</description><subject>Agricultural biotechnology</subject><subject>Aqueous solutions</subject><subject>Biochemistry</subject><subject>Biological and medical sciences</subject><subject>Biomass</subject><subject>Bioreactors</subject><subject>Bioreactors - microbiology</subject><subject>Biotechnology</subject><subject>Cell Culture Techniques - methods</subject><subject>Cellulose</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Computer Simulation</subject><subject>Culture Media - chemistry</subject><subject>Ethanol</subject><subject>Fermentation</subject><subject>Fluid dynamics</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Hydrodynamics</subject><subject>Methods. Procedures. Technologies</subject><subject>Microbial engineering. 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This mixture is not only costly to separate but also produces a large aqueous stream that must then be disposed of or recycled. Integrative approaches to water reduction include increasing the biomass concentration during fermentation. In this paper, experimental results are presented for the rheological behavior of high-solids enzymatic cellulose hydrolysis and ethanol fermentation for biomass conversion using Solka Floc as the model feedstock. The experimental determination of the viscosity, shear stress, and shear rate relationships of the 10 to 20% slurry concentrations with constant enzyme concentrations are performed with a variable speed rotational viscometer (2.0 to 200 rpm) at 40 °C. The viscosities of enzymatic suspension observed were in range of 0.0418 to 0.0144, 0.233 to 0.0348, and 0.292 to 0.0447 Pa s for shear rates up to 100 reciprocal seconds at 10, 15, and 20% initial solids (w/v), respectively. Computational fluid dynamics analysis of bioreactor mixing demonstrates the change in bioreactor mixing with increasing biomass concentration. The portion-loading method is shown to be effective for processing high-solids slurries.</abstract><cop>New York</cop><pub>Humana Press Inc</pub><pmid>18425609</pmid><doi>10.1007/s12010-007-8105-z</doi><tpages>10</tpages></addata></record> |
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subjects | Agricultural biotechnology Aqueous solutions Biochemistry Biological and medical sciences Biomass Bioreactors Bioreactors - microbiology Biotechnology Cell Culture Techniques - methods Cellulose Chemistry Chemistry and Materials Science Computer Simulation Culture Media - chemistry Ethanol Fermentation Fluid dynamics Fundamental and applied biological sciences. Psychology Hydrodynamics Methods. Procedures. Technologies Microbial engineering. Fermentation and microbial culture technology Models, Chemical Rheology - methods Shear stress Slurries Solids Various methods and equipments Viscosity Zymomonas - chemistry Zymomonas mobilis |
title | A Comparison of Simple Rheological Parameters and Simulation Data for Zymomonas mobilis Fermentation Broths with High Substrate Loading in a 3-L Bioreactor |
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