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Continuous co-production of ethanol and xylitol from rice straw hydrolysate in a membrane bioreactor
by
Jouzani, Gholamreza Salehi
, Tabatabaei, Meisam
, Khodaiyan, Faramarz
, Abbasalizadeh, Saeed
, Zahed, Omid
in
Acetic acid
/ Applied Microbiology
/ batch fermentation
/ Biomass
/ Biomedical and Life Sciences
/ Bioreactors
/ Biorefineries
/ biorefining
/ Biotransformation
/ Candida tropicalis
/ carbon
/ Cellulose - metabolism
/ coculture
/ Detoxification
/ Environmental Engineering/Biotechnology
/ enzymatic hydrolysis
/ Ethanol
/ Ethanol - metabolism
/ ethanol production
/ Fermentation
/ furfural
/ hydrolysates
/ Hydrolysis
/ hydroxymethylfurfural
/ Immunology
/ Kinetics
/ Life Sciences
/ lignocellulose
/ Membrane reactors
/ Microbiology
/ Nitrogen - metabolism
/ Oryza - metabolism
/ Oryza - microbiology
/ Oxygen - metabolism
/ Rice
/ Rice straw
/ Saccharomyces cerevisiae
/ Saccharomyces cerevisiae - metabolism
/ Studies
/ Sugar
/ Sulfuric Acids - metabolism
/ value-added products
/ wastes
/ xylitol
/ Xylitol - metabolism
/ Yeasts
2016
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Continuous co-production of ethanol and xylitol from rice straw hydrolysate in a membrane bioreactor
by
Jouzani, Gholamreza Salehi
, Tabatabaei, Meisam
, Khodaiyan, Faramarz
, Abbasalizadeh, Saeed
, Zahed, Omid
in
Acetic acid
/ Applied Microbiology
/ batch fermentation
/ Biomass
/ Biomedical and Life Sciences
/ Bioreactors
/ Biorefineries
/ biorefining
/ Biotransformation
/ Candida tropicalis
/ carbon
/ Cellulose - metabolism
/ coculture
/ Detoxification
/ Environmental Engineering/Biotechnology
/ enzymatic hydrolysis
/ Ethanol
/ Ethanol - metabolism
/ ethanol production
/ Fermentation
/ furfural
/ hydrolysates
/ Hydrolysis
/ hydroxymethylfurfural
/ Immunology
/ Kinetics
/ Life Sciences
/ lignocellulose
/ Membrane reactors
/ Microbiology
/ Nitrogen - metabolism
/ Oryza - metabolism
/ Oryza - microbiology
/ Oxygen - metabolism
/ Rice
/ Rice straw
/ Saccharomyces cerevisiae
/ Saccharomyces cerevisiae - metabolism
/ Studies
/ Sugar
/ Sulfuric Acids - metabolism
/ value-added products
/ wastes
/ xylitol
/ Xylitol - metabolism
/ Yeasts
2016
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Continuous co-production of ethanol and xylitol from rice straw hydrolysate in a membrane bioreactor
by
Jouzani, Gholamreza Salehi
, Tabatabaei, Meisam
, Khodaiyan, Faramarz
, Abbasalizadeh, Saeed
, Zahed, Omid
in
Acetic acid
/ Applied Microbiology
/ batch fermentation
/ Biomass
/ Biomedical and Life Sciences
/ Bioreactors
/ Biorefineries
/ biorefining
/ Biotransformation
/ Candida tropicalis
/ carbon
/ Cellulose - metabolism
/ coculture
/ Detoxification
/ Environmental Engineering/Biotechnology
/ enzymatic hydrolysis
/ Ethanol
/ Ethanol - metabolism
/ ethanol production
/ Fermentation
/ furfural
/ hydrolysates
/ Hydrolysis
/ hydroxymethylfurfural
/ Immunology
/ Kinetics
/ Life Sciences
/ lignocellulose
/ Membrane reactors
/ Microbiology
/ Nitrogen - metabolism
/ Oryza - metabolism
/ Oryza - microbiology
/ Oxygen - metabolism
/ Rice
/ Rice straw
/ Saccharomyces cerevisiae
/ Saccharomyces cerevisiae - metabolism
/ Studies
/ Sugar
/ Sulfuric Acids - metabolism
/ value-added products
/ wastes
/ xylitol
/ Xylitol - metabolism
/ Yeasts
2016
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Continuous co-production of ethanol and xylitol from rice straw hydrolysate in a membrane bioreactor
Journal Article
Continuous co-production of ethanol and xylitol from rice straw hydrolysate in a membrane bioreactor
2016
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Overview
The present study was set to develop a robust and economic biorefinery process for continuous co-production of ethanol and xylitol from rice straw in a membrane bioreactor. Acid pretreatment, enzymatic hydrolysis, detoxification, yeast strains selection, single and co-culture batch fermentation, and finally continuous co-fermentation were optimized. The combination of diluted acid pretreatment (3.5 %) and enzymatic conversion (1:10 enzyme (63 floating-point unit (FPU)/mL)/biomass ratio) resulted in the maximum sugar yield (81 % conversion). By concentrating the hydrolysates, sugars level increased by threefold while that of furfural reduced by 50 % (0.56 to 0.28 g/L). Combined application of active carbon and resin led to complete removal of furfural, hydroxyl methyl furfural, and acetic acid. The strains
Saccharomyces cerevisiae
NCIM 3090 with 66.4 g/L ethanol production and
Candida tropicalis
NCIM 3119 with 9.9 g/L xylitol production were selected. The maximum concentrations of ethanol and xylitol in the single cultures were recorded at 31.5 g/L (0.42 g/g yield) and 26.5 g/L (0.58 g/g yield), respectively. In the batch co-culture system, the ethanol and xylitol productions were 33.4 g/L (0.44 g/g yield) and 25.1 g/L (0.55 g/g yield), respectively. The maximum ethanol and xylitol volumetric productivity values in the batch co-culture system were 65 and 58 % after 25 and 60 h, but were improved in the continuous co-culture mode and reached 80 % (55 g/L) and 68 % (31 g/L) at the dilution rate of 0.03 L per hour, respectively. Hence, the continuous co-production strategy developed in this study could be recommended for producing value-added products from this hugely generated lignocellulosic waste.
Publisher
Springer Netherlands,Springer Nature B.V
Subject
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