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生物接触氧化法处理富马酸废水
引用本文:彭绍玲,伍钦.生物接触氧化法处理富马酸废水[J].华南理工大学学报(自然科学版),2004,32(5):71-73,79.
作者姓名:彭绍玲  伍钦
作者单位:华南理工大学,化工学院,广东,广州,510640
摘    要:采用好氧生物膜接触氧化法处理富马酸废水,用盾式纤维填料作为生物的支持物,研究生物降解富马酸的原理和不同工艺条件对富马酸废水降解的影响.实验结果表明,富马酸的降解符合一级反应规律,最佳的反应气水比为16,控制水力停留时间为8h.当富马酸废水COD和BOD,分别增至l800mg/L和520mg/L时,处理后的废水的COD约为216mg/L,BOD,约为114mg/L,BOD,与COD的比值为0.53.在反应器容积负荷提高到原来的7.6倍,运行40h后,COD去除率约可恢复到70%,表明生物膜接触氧化反应器具有较大的缓冲能力,其抗冲击负荷能力较强。

关 键 词:富马酸  废水  生物膜  生物接触氧化法
文章编号:1000-565X(2004)05-0071-03

Treatment of Fumaric Acid-containing Wastewater by Bio-contact Oxidation
Peng Shao-ling,Wu Qin.Treatment of Fumaric Acid-containing Wastewater by Bio-contact Oxidation[J].Journal of South China University of Technology(Natural Science Edition),2004,32(5):71-73,79.
Authors:Peng Shao-ling  Wu Qin
Abstract:This paper deals with the treatment of fumaric acid-containing wastewater by using the aerobic biofilm contact oxidation, that is, to degrade the fumaric acid in wastewater by using peltate fibre filling as the biological support, thus expounding the mechanism and technology of treating wastewater. Experimental results indicate that the degradation of fumaric acid wastewater accords with the first order reaction principle; that the optimal ratio of the gas to water is 16 and the hydrodynamic retention time is 8h; that when the inlet COD and BOD 5 are respectively up to 1800 mg/L and 520 mg/L, under stable conditions, the outlet COD and BOD 5 of the reactor are respectively 216 mg/L and 114 mg/L, while the B/C value is 0.53; and that when the cubage load increases by 6.6 times, the COD removal of the reactor will approach to 70% after working for 40 h, which reveals that the reactor for aerobic film contact oxidation is of excellent buffering ability and strong impact resistance ability.
Keywords:fumaric acid  wastewater  biofilm  bio-contact oxidation
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