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出 处:《科学技术与工程》2007年第6期1119-1122,共4页Science Technology and Engineering
基 金:河南省科技攻关项目(0424440066)资助
摘 要:采用两相厌氧生物处理工艺的产酸相作为硫酸盐还原单元,以食用红糖为碳源,通过连续流实验,重点研究了产酸相中COD/SO42-值(C/S)对SO42-去除率的影响。在(34±1)℃、进水碱度(ALK)(300~500)mg/L、pH(6.0~6.2)、氧化还原电位(ORP)(-250^-350)mV等条件下,当进水C/S<2.0时,SO24-去除率小于81%;当进水C/S值为2.5~2.0时,SO42-去除率为(90~81)%;当进水C/S值为大于2.5时,SO24-去除率为90%以上。随着C/S值的降低,SO24-的去除效果会将有所降低。In order to investigate the effect of COD/SO4^2- (C/S)ratio on sulfate removal rate in an acidogenic phase reactor of two-phase anaerobic bio-treatment system,a group of continuous-flow experiments were conducted in an acidogenic sulfate-reducing reactor in which red-sugar was the source of COD . The operation conditions of the reactor was controlled as follows : temperature at ( 34 ± 1 ) ℃, influent alkalinity (ALK) at 300 mg/L to 500 rag/L, at pH6.0 to pH6.2 ,oxidation reduction potential(ORP) at -250 mV to -350 mV. It was demonstrated that the sulfate removal rate would be less than 81% when the influent C/S ratio was less than 2.0,and 81% to 90% suflate removal rate could achieved when the influent C/S ratio was at 2.0 to 2.5, and more than 90% when C/S rate was more than 2.5. In conclusion ,with the influent C/S ratio reduced, the sulfate removal rate reduced ,too.
关 键 词:产酸脱硫反应器 COD/SO4^2-比 SO4^2-去除率 硫酸盐还原菌(SRB)
分 类 号:X763.5[环境科学与工程—环境工程]
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