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Evaluation of Design and Operational Parameters of Pilot Single Stage Stabilization Pond for Treatment of Brewery Waste Water Effluent

机译:啤酒废水处理用单级试验稳定池设计及运行参数评价。

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The suitability of waste stabilization pond (WSP) as a cheaper alternative in the treatment of brewery wastewater effluent was investigated. A pilot WSP was designed and constructed and test run for the treatment brewery wastewater effluent. Wastewater effluents were collected from an operating brewing industry in Kudenda light industrial layout, Kaduna. The influent pond flow rate of 0.2 m3/day was chosen for the design of the pilot pond. Kinetic model design procedure of a facultative pond was used to design a rectangular shaped pond to reduce the BOD loading by 90%. The pond capacity was 4.7 m3 (4700 litres) with a retention time of 25 days. The parameters that were analyzed for the raw and treated wastewater include: Biological Oxygen Demand (BOD5), Chemical Oxygen Demand (COD), Total suspended solids (TSS), Turbidity and Electrical conductivity (EC). It was observed that aerobic degradation occurred at the upper layer of the pond favoring the activities of aerobic bacteria. At the middle layer however favored the activities of the facultative bacteria, while at the lower level where there is virtually little or no presence of dissolved oxygen, anaerobic decomposition of the wastewater predominate. These combined mechanisms yielded the total the total decomposition of the wastewater by the pond. The BOD removal rate constant was 0.088 per day and the BOD-COD correlation was BOD=0.531COD-1.960. The BOD removal regression model was: BOD=0.0001t5-0.0034t4-0.1419t3+6.6096t2-102.09t+1114.5 and the pond performance efficiencies for the reduction/removal of the tested parameters 69% 68.9%, 81%, 67.2% and 71.6% respectively. The pond performance was found to be satisfactory and the kinetic parameter obtained can be utilized in the scale up design for industrial scale WSP.
机译:废物稳定池(WSP)作为啤酒厂废水处理中较便宜的替代品的适用性进行了研究。设计并建造了水处理厂试点,用于处理啤酒厂废水。废水是从位于卡杜纳(Kaduna)的库登达(Kudenda)轻工业布局的酿酒厂中收集的。选择试验池的进水流量为0.2 m3 /天。采用兼性池的动力学模型设计程序设计矩形池,以将BOD负荷降低90%。池塘容量为4.7立方米(4700升),保留时间为25天。对原废水和处理过的废水进行分析的参数包括:生物需氧量(BOD5),化学需氧量(COD),总悬浮固体(TSS),浊度和电导率(EC)。观察到有氧降解发生在池塘的上层,有利于需氧细菌的活动。然而,在中间层有利于兼性细菌的活动,而在较低水平(实际上几乎没有或根本没有溶解氧),废水的厌氧分解占主导地位。这些综合的机制产生了池塘中废水的全部分解。 BOD去除率常数为每天0.088,BOD-COD相关性为BOD = 0.531COD-1.960。 BOD去除回归模型为:BOD = 0.0001t5-0.0034t4-0.1419t3 + 6.6096t2-102.09t + 1114.5和池塘性能降低/去除测试参数的效率为69%68.9%,81%,67.2%和分别为71.6%。发现该池塘的性能令人满意,并且所获得的动力学参数可用于工业规模WSP的按比例放大设计。

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