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Optimization of operation conditions for the start-up of a pilot-scale anaerobic biofilm digester treating leachate

机译:优化操作条件以启动中试规模的厌氧生物膜消化池处理渗滤液

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In solid waste management, treating putrid leachate is the most challenging part especially for Malaysia, which has hot and humid weather and raining season throughout the year. Leachate pollution has become a more serious problem these recent years as lack of proper treatment facilities at waste disposal sites affected the quality of water supply due to the penetration of leachate into the groundwater table and its discharge into the rivers. Anaerobic treatment has recently been mentioned by the Malaysian government as the most sustainable technology for waste treatment. Hence, the objective of this study is to optimize the operation conditions for the start-up of a pilot-scale anaerobic biofilm digester at UKM Biogas Site for leachate treatment. In this paper, the results of two separate preliminary operations of anaerobic digestion of leachate are presented. The first operation, conducted with 20-d HRT (daily feed 0.30 m(3)/d) and pH adjustment, was halted after 35 d due to the hydraulic and organic overloads, resulting into system failure. The results were taken into account while commencing the second operation by using the buffering step where small amount of leachate was fed for a month (0.03 m(3)/d for the first week and 0.06 m(3)/d for the rest weeks), with no pH adjustment. This buffering step was conducted to enable the microbes to acclimatize to leachate's low pH and its high organic contents. This step was proven better as parameters observed (pH, total suspended solids, volatile suspended solids, chemical oxygen demand, NH3-N, total volatile fatty acids) showed more consistent values than those of the first operation.
机译:在固体废物管理中,处理腐烂的渗滤液是最具挑战性的部分,特别是对于马来西亚而言,马来西亚全年天气炎热潮湿,雨季多。近年来,由于渗滤液渗入地下水位并排入河流,垃圾处理场缺乏适当的处理设施,影响了供水质量,渗滤液已成为一个更为严重的问题。最近,马来西亚政府将厌氧处理称为废物处理的最可持续技术。因此,本研究的目的是优化UKM沼气厂中试规模厌氧生物膜消化池启动以进行渗滤液处理的操作条件。本文介绍了两种单独的厌氧消化浸出液的初步操作的结果。第一次操作是在20天HRT(每日进料0.30 m(3)/ d)和pH值调整的情况下进行的,由于液压和有机物过载,在35 d后中止了操作,从而导致系统故障。开始使用缓冲步骤进行第二次操作时要考虑到结果,在该步骤中,每月要补给少量渗滤液(第一周为0.03 m(3)/ d,其余几周为0.06 m(3)/ d ),无需调整pH值。进行该缓冲步骤以使微生物适应沥滤液的低pH值和其高有机含量。与观察到的参数(第一个操作)相比,该步骤更好地证明了所观察到的参数(pH,总悬浮固体,挥发性悬浮固体,化学需氧量,NH3-N,总挥发性脂肪酸)的一致性。

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