Production of ethanol from starch by co-immobilized Zymomonas mobilis-glucoamylase in a fluidized-bed reactor

被引:12
作者
Sun, MY
Nghiem, NP
Davison, BH
Webb, OF
Bienkowski, PR
机构
[1] Oak Ridge Natl Lab, Bioproc Res & Dev Ctr, Oak Ridge, TN 37831 USA
[2] Univ Tennessee, Dept Chem Engn, Knoxville, TN 37916 USA
关键词
ethanol; starch; Zymomonas mobilis; glucoamylase; simultaneous saccharification and fermentation; fluidized-bed reactor;
D O I
10.1007/BF02920158
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
The production of ethanol from starch was studied in a fluidized-bed reactor (FBR) using co-immobilized Zymomonas mobilis and glucoamylase. The FBR was a glass column of 2.54 cm in diameter and 120 cm in length. The Z. mobilis and glucoamylase were co-immobilized within small uniform beads (1.2-2.5 mm diameter) of kappa-carrageenan. The substrate for ethanol production was a soluble starch. Light steep water was used as the complex nutrient source. The experiments were performed at 35 degrees C and pH range of 4.0-5.5. The substrate concentrations ranged from 40 to 185 g/L, and the feed rates from 10 to 37 mL/min. Under relaxed sterility conditions, the FBR was successfully operated for a period of 22 d, during which no contamination or structural failure of the biocatalyst beads was observed. Volumetric productivity as high as 38 g ethanol/(Lh), which was 74% of the maximum expected value, was obtained. Typical ethanol volumetric productivity was in the range of 15-20 g/(Lh). The average yield was 0.49 g ethanol/g substrate consumed, which was 90% of the theoretical yield. Very low levels of glucose were observed in the reactor, indicating that starch hydrolysis was the rate-limiting step.
引用
收藏
页码:429 / 439
页数:11
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