厌氧消化
肥料
沼气
氨
水力停留时间
动物科学
产量(工程)
化学
无氧运动
废物管理
环境科学
生物
农学
环境工程
废水
生物化学
甲烷
工程类
有机化学
冶金
材料科学
生理学
作者
Kaare Hvid Hansen,İrini Angelidaki,Birgitte K. Ahring
出处
期刊:Water Research
[Elsevier BV]
日期:1998-01-01
卷期号:32 (1): 5-12
被引量:1152
标识
DOI:10.1016/s0043-1354(97)00201-7
摘要
A stable anaerobic degradation of swine manure with ammonia concentration of 6 g-N/litre was obtained in continuously stirred tank reactors with a hydraulic retention time of 15 days, at four different temperatures. Methane yields of 188, 141, 67 and 22 ml-CH 4 /g-VS were obtained at 37, 45, 55 and 60°C, respectively. The yields were significantly lower than the potential biogas yield of the swine manure used (300 ml-CH 4 /g-VS). A free ammonia concentration of 1.1 g-N/litre or more was found to cause inhibition in batch cultures at pH 8.0 (reactor pH), and higher free ammonia concentrations resulted in a decreased apparent specific growth rate. Batch experiments with various mixtures of swine and cattle manure showed that the biogas process was inhibited when the swine-to-cattle manure ratio was higher than 25:75, corresponding to a free ammonia concentration of approximately 1.1 g-N/litre. Inhibition of the biogas process and, thereby, a reduction of the methane yield followed a four-stage pattern: below a threshold of 1.1 g-N/litre free ammonia, the process was uninhibited; over this concentration, inhibition occurred, forming first a phase with an initial inhibition, then a plateau and then an inhibition stage where the apparent specific growth rate decreased with increasing concentrations of free ammonia. © 1998 Elsevier Science Ltd. All rights reserved
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