Liu Qiang, Xu Hui, Li Mi, Xu Zhi-yi, Qian Guang-ren
School of Environment and Chemical Engineering, Shanghai University, Shanghai 200444, China.
Huan Jing Ke Xue. 2009 Aug 15;30(8):2491-6.
An expanded granular sludge bed reactor (EGSB) was employed to evaluate the start-up process of fermentative biohydrogen production from compost leachate. The removal performance of COD, total nitrogen, total phosphorus in leachate as well as the hydrogen production ability of EGSB was investigated. The results showed that at 35 degrees C +/- 1 degrees C, organic loading rate of 1.4-16.7 g/(L x d), the main pH of 5.0 to 5.5, the continuous hydrogen production by EGSB reactor using the compost leachate as substrate could be achieved after 20d's acclimatization. Under conditions of HRT of 30 h and liquid flow rate of 3.0 m/h, the COD removal rate of between 50% to 70%, the content of hydrogen in the biogas of between 19%-33%, the maximal hydrogen production rate of 1 460 mL/(L x d), total phosphorus and total nitrogen removal rate of between 40%-70% and 32%-65% respectively, were achieved.The total ethanol and acetic acid content was more than 80% in liquid end products (VFAs), suggesting the main fermentation is ethanol fermentation type.
采用膨胀颗粒污泥床反应器(EGSB)评估以堆肥渗滤液为原料发酵生物制氢的启动过程。研究了渗滤液中化学需氧量(COD)、总氮、总磷的去除性能以及EGSB的产氢能力。结果表明,在35℃±1℃、有机负荷率为1.4-16.7g/(L·d)、主要pH值为5.0至5.5的条件下,以堆肥渗滤液为底物的EGSB反应器经20天驯化后可实现连续产氢。在水力停留时间(HRT)为30小时、液体流速为3.0m/h的条件下,COD去除率为50%至70%,沼气中氢气含量为19%-33%,最大产氢率为1460mL/(L·d),总磷和总氮去除率分别为40%-70%和32%-65%。液体终产物(挥发性脂肪酸,VFAs)中乙醇和乙酸的总含量超过80%,表明主要发酵类型为乙醇发酵型。