通过化学应用改善城市污水处理厂

H. Park, S.Y. Lee, Y.H. Kim
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引用次数: 0

摘要

通过全规模和半中试试验,研究了两个模型厂对城市污水处理厂的强化效果。将20 60p1/1的Hi-PAX(聚氯化铝硅酸盐,A1203 17%)简单应用于一级污水处理厂的进水泵入口(250000 m3/天),对所有污染物的去除效率均有所提高。SS去除率由40%提高到81%,BOD和COD去除率分别由30%提高到71%和29%提高到57%。此外,总氮和总磷的去除率也分别由3%和29%提高到27%和96%。采用半中试装置评价了化学预沉淀对生物处理效果的影响,在预沉淀步骤中添加15pVl的Hi-PAX可提高有机物、氮、磷的去除率。此外,增加初级沉淀中有机物的去除率可使后续生物步骤的F/M比降低约30%,使曝气池的需氧量降低约50%。截至1997年底,全国共有污水处理设施93个,总处理量1504万吨/日,污水处理率为60.9%。然而,标准活性污泥工艺(90%)是最广泛使用的,除了一些地方使用延长曝气(2%),旋转生物接触器(3%)和只使用初级沉淀(5%)(韩国教育部,1996年)。1996年《水质保护法修正案》的影响反映了公众对清洁水环境的渴望。将BOD、COD和SS的出水标准分别由30 mg/l、50mg/l和70mg/l提高到20mg/l、40mg/l和20mg/l,并在出水标准中增加了总氮(T-N, 60mg/l)和总磷(T-P, 8mg/l)。由于加强了BOD、COD、S、T-N和T-P的出水标准,人们对改进和扩大现有处理厂和新工艺以达到预期的更严格的出水标准的兴趣日益增加。(0 degaard化学应用。H.和卡尔森。I. 1994)已以各种方式用于改善废水处理,例如唯一的处理过程(初级沉淀或直接沉淀),以及在预沉淀,同时沉淀和后沉淀方面与生物处理相结合。然而,在应用化学改造技术之前,必须充分考虑许多因素,如污染成分和程度的变化、使用的技术类型、工业和生活污水的类型和混合以及地表水的数量。因此,选择两个示范装置进行市政0-7803-5729-9/99/$10.00化工升级的可行性研究
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Enhancement of municipal wastewater treatment plants by chemical application
The enhancement of municipal wastewater treatment plant was investigated at the two model plants by full scale and semi-pilot scale experiments. The simple application of 20 0 60p1/1 of Hi-PAX(Po1y Aluminum Chloride Silicate, A1203 17%) to the inlet of the influent pump of the primary sewage treatment plant(250,OOO m3/day) showed enhanced removal eficiencies in all contaminants. The removal rate of SS increased from 40% to 81%, while that of BOD and COD from 30% to 71% and 29% to 57%, respectively. In addition, the removal rate of total nitrogen and phosphorous also increased from 3% and 29% to 27% and 96%, respectively. The effect of chemical pre-precipitation on the biological treatment was evaluated by semi-pilot plant with and without pre-precipitation step, The addition of 15pVl of Hi-PAX to the preprecipitation step could enhance the removal efficiencies of S S , organic matters, nitrogen and phosphorus. In addition, the increased removal of organic matters in the primary sedimentation could reduce the F/M ratio of the following biological step by about 30% and reduce the oxygen requirement in the aeration tank by about 50%. Introduction As the end of 1997, there were 93 sewage treatment facilities in Korea with the total capacity of 15.04 million tons/day, and the sewage treatment ratio was 60.9%. However the standard activated sludge process(90%) is the most widely used, except for a number of places where extended aeration(2%), rotating biological contactor(3%) and only primary sedimentation(5%) are used(Korea MOE, 1996). The implications of the 1996 Amendments to the Water Quality Protection Act reflected the desire of the public for the clean water environment. The effluent standards for BOD, COD and SS were tightened from 30 mg/l , 50mg/l and 70mg/l to 20 mg/l, 40mg/l and 20mg/l, respectively, and two new pollutants total nitrogen(T-N, 60mg/l) and total phosphorus(T-P, 8mg/l)-were added to the effluent standards. Due to the strengthening effluent standards for BOD, COD, S S , T-N and T-P, interest in the improvement and expansion of the existing treatment plants and new processes for the anticipated more stringent effluent standards are increasingly growing up. Chemical application(0degaard. H. and Karlson. I. 1994) has been used in various ways to improve the wastewater treatment such as the only treatment process(Primary precipitation or direct precipitation) and in combination with biological treatment in terms of pre-, simultaneousand postprecipitation. However, many factors, such as the variation in composition and degree of pollution, the type of technologies in use, the type and mix of industrial and domestic sewage, and the amount of surface water, must be fully considered before applying the chemical upgrading technologies. Thus two model plants are selected for the feasibility study of chemical upgrading of municipal 0-7803-5729-9/99/$10.00
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