Ethanol-type fermentation from carbohydrate in high rate acidogenic reactor

被引:3
|
作者
Ren, NQ [1 ]
Wang, BZ [1 ]
Huang, JC [1 ]
机构
[1] HONG KONG UNIV SCI & TECHNOL,KOWLOON,HONG KONG
关键词
fermentation; two-stage anaerobic waste treatment; acidogenic reactor; fermentation type; hydrogen partial pressure; ethanol-type fermentation;
D O I
10.1002/(SICI)1097-0290(19970605)54:5<428::AID-BIT3>3.3.CO;2-U
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
It has been found, in this study, that a new ethanol-type fermentation can be obtained in a continuous flow, high-rate acidogenic reactor receiving molasses as the feed. The operating pH must be maintained at about 4.5 to avoid onset of propionic fermentation. The acidogenic reactor had a VSS level of 20 g/L and its organic loading was as high as 80 to 90 kg COD/m(3) d. The operating ORP was around -250 mV. The ethanol-type fermentation was characterized by a simultaneous production of acetic acid and ethanol, while the yield of propionic was minimal even at a high organic loading rate of 80 to 90 kg COD/m(3) d, and also, the hydrogen partial pressure was as high as 50 kPa. Thus, this study has shown that the production of propionic acid is not always related to high hydrogen partial pressure. When the operating pH was increased to 5.5, the yield of propionic acid became significant. (C) 1997 John Wiley & Sons, Inc.
引用
收藏
页码:428 / 433
页数:6
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