Continuous co-production of ethanol and xylitol from rice straw hydrolysate in a membrane bioreactor
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- 作者：Omid Zahed ; Gholamreza Salehi Jouzani ; Saeed Abbasalizadeh…
- 刊名：Folia Microbiologica
- 出版年：2016
- 出版时间：May 2016
- 年：2016
- 卷：61
- 期：3
- 页码：179-189
- 全文大小：611 KB
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Gholamreza Salehi Jouzani (1)
Saeed Abbasalizadeh (1)
Faramarz Khodaiyan (2)
Meisam Tabatabaei (1) (3)
1. Microbial Biotechnology and Biosafety Department, Agricultural Biotechnology Research Institute of Iran (ABRII), SPII Campus, Mahdasht Road, Karaj, P.O. Box: 31535-1897, Iran
2. Department of Food Science, Engineering and Technology, Faculty of Agricultural Engineering and Technology, University of Tehran, Karaj, Iran
3. Biofuel Research Team (BRTeam), Karaj, Iran - 刊物主题：Life Sciences, general; Microbiology; Applied Microbiology; Immunology; Environmental Engineering/Biotechnology;
- 出版者：Springer Netherlands
- ISSN：1874-9356
文摘
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.