摘要
以30g/L葡萄糖合成废水为原料,研究了厌氧酸化的操作温度(θ)对酸化率的影响,确定了达到最佳酸化产物分布时的pH值,并以酸化反应器的出水为碳源,在5L发酵罐上进行了分批和流加发酵实验.结果表明,θ=40℃时,废水的酸化率接近100%;控制pH5.7,停留时间10h可使丁酸占UASB反应器出水中总酸质量的68%;与分批发酵相比,流加发酵法可大幅度地提高PHA的产量,发酵54h后,DCW和PHA的质量浓度可分别达到15.8g/L和10g/L.
The effect of temperature on the degree of acidification and that of pH on the organic acids distribution in the effluent of UASB were investigated. The batch and fed batch fermentations were carried out in a 5 L fermentor with acidified wastewater as carbon source. The results showed that the degree of acidification was almost 100% when temperature was 40℃. When pH was controlled at 5.7, butyric acid accounted for 68% of the total acids in the effluent of UASB. PHA production could be improved greatly in fed-batch fermentation compared with that in batch fermentation, DCW and PHA reached 15.8 g/L and 10 g/L, respectively after 54 h.
出处
《应用与环境生物学报》
CAS
CSCD
1999年第4期400-403,共4页
Chinese Journal of Applied and Environmental Biology
基金
国家自然科学基金
国家教委优秀青年教师项目
关键词
厌氧酸化
聚羟基烷酸
分批发酵
有机废水
anaerobic acidification
polyhydroxyalkanoate
batch fermentation
fed batch fermentation