Control of Start-up and Operation in Continuous Fermentation of Bio-Hydrogen Production Reactor

被引:0
|
作者
Qin, Zhi [1 ]
Qin, Dan [1 ]
Li, Dan [1 ]
机构
[1] Harbin Univ Sci & Technol, Sch Chem & Environm Engn, Harbin 150040, Peoples R China
关键词
Start-up; Bio-hydrogen production; Anaerobic fermentation; CSTR Reactor;
D O I
10.4028/www.scientific.net/AMR.183-185.552
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
Bio-hydrogen production from diluted molasses by anaerobic activated sludge was investigated in a continuous stirred-tank reactor (CSTR) under condition of continuous flow in this study. Research shows that the reactor started up under the condition of influent COD concentration 3000mg/L, HRT8h, pH6.5 similar to 7.5 and (35 +/- 1) degrees C. The process performed steadily and a dominant butyric acid and acetic acid type fermentation population was established, acetic acid and butyric acid accounted for about 80% in the liquid fermentation products. The effluent PH value was maintained about 5.0. The biogas yield could reach at 4.87L/d while hydrogen yield reached 41.25mL/d under the condition. When influent COD concentration rose to 5500 mg/L, the biogas yield and hydrogen yield as high as 9.45L/d and 119.98mL/d were obtained.
引用
收藏
页码:552 / 556
页数:5
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