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在气升式生物反应器中利用稻草水解液生产微生物生物量。

Microbial biomass production from rice straw hydrolysate in airlift bioreactors.

作者信息

Zheng Yu-Guo, Chen Xiao-Long, Wang Zhao

机构信息

Institute of Bioengineering, Zhejiang University of Technology, Hangzhou 310014, PR China.

出版信息

J Biotechnol. 2005 Sep 10;118(4):413-20. doi: 10.1016/j.jbiotec.2005.04.022.

DOI:10.1016/j.jbiotec.2005.04.022
PMID:15978690
Abstract

Rice straw is a by-product of rice production, and a great bioresource as raw biomass material for manufacturing value-adding protein for animal feedstock, which has been paid more and more attention. In the present work, utilizing rice straw hydrolysate as a substrate for microbial biomass production in 11.5L external-loop airlift bioreactors was investigated. Rice straw hydrolysate obtained through acid-hydrolyzing rice straw was used for the culture of yeast Candida arborea AS1.257. The influences of gas flow rate, initial liquid volume, hole diameter of gas sparger and numbers of sieve plates on microbial biomass production were examined. The best results in the external-loop airlift bioreactor were obtained under 9.0 L initial liquid volume, 1.1 (v/v)/min gas flow rate during culture time of 0-24 h and 1.4 (v/v)/min gas flow rate of 24-48 h at 29+/-1 degrees C. The addition of the sieve plates in the riser of the external-loop airlift bioreactor increased productivity. After 48 h, under optimized operation conditions, crude protein productivity with one sieve and two sieves were 13.6 mg/mL and 13.7 mg/mL, respectively, comparing 12.7 mg/mL without sieves in the airlift bioreactor and 11.7 mg/mL in the in the 10-L mechanically stirred tank bioreactor. It is feasible to operate the external-loop airlift bioreactors and possible to reduce the production cost for microbial biomass production from the rice straw hydrolysate.

摘要

稻草是水稻生产的副产品,作为制造动物饲料增值蛋白质的生物质原料,是一种重要的生物资源,已受到越来越多的关注。在本研究中,考察了以稻草水解液为底物,在11.5L外循环气升式生物反应器中生产微生物生物质的情况。通过酸水解稻草得到的稻草水解液用于培养酵母树状假丝酵母AS1.257。考察了气体流速、初始液体体积、气体分布器孔径和筛板数量对微生物生物质产量的影响。在外循环气升式生物反应器中,在初始液体体积为9.0L、0-24h培养时间内气体流速为1.1(v/v)/min、24-48h气体流速为1.4(v/v)/min、温度为29±1℃的条件下,获得了最佳结果。在外循环气升式生物反应器的上升管中添加筛板提高了生产率。48h后,在优化的操作条件下,有一个筛板和两个筛板的粗蛋白生产率分别为13.6mg/mL和13.7mg/mL,相比之下,气升式生物反应器中无筛板时为12.7mg/mL,10L机械搅拌罐式生物反应器中为11.7mg/mL。操作外循环气升式生物反应器是可行的,并且有可能降低利用稻草水解液生产微生物生物质的成本。

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