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作 者:王仁桃[1,2] 任云霞[1] 刘黎[1] 董桂燕[1] 李永旺[1]
机构地区:[1]中国科学院山西煤炭化学研究所,山西太原030001 [2]中国科学院研究生院,北京100049
出 处:《燃料化学学报》2011年第4期307-310,共4页Journal of Fuel Chemistry and Technology
基 金:国家杰出青年科学基金(20625620)
摘 要:采用厌氧悬浮填料生物膜反应器工艺对费托合成废水进行处理,考察了高有机负荷条件下系统的运行情况。有机负荷小于31.1g/(L.d)时,COD去除率达97%以上;当有机负荷从39.7g/(L.d)增加至56.3g/(L.d)时,厌氧反应对COD的去除率从88%降至61%。实验结果表明,填料生物膜比悬浮污泥具有更高的活性,MBBR系统具有运行稳定、抗冲击力强的优点。The objective of this paper is to investigate COD removal efficiency of the Fischer-Tropsch-processing wastewater by applying the anaerobic moving-bed biofilm reactor(MBBR).The contribution of the anaerobic MBBR to total COD removal efficiency reached 97% at an organic loading rate(OLR) of 31.1g/(L·d).The COD removal efficiency of the anaerobic system had a slight decrease to 88% even though the feed OLR was increased to 39.7g/(L·d),and gradually decreased to 61% when feed OLR was increased to 56.3g/(L·d).The COD removal results in the anaerobic batch experiments of biofilm and sludge showed that the attached biofilm has higher activity than suspended sludge.The anaerobic MBBR system showed a characteristic of steady performance and resistance ability during the operation period.
关 键 词:悬浮填料生物膜反应器 费托合成废水 COD去除率 生物活性
分 类 号:X703[环境科学与工程—环境工程]
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