Studies on biodegradation of organic waste in uasb reactor

C. Majumder, A. K. Mathur, V. Kapse
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Abstract

The industrialization in the developing countries causes severe problems in collection,treatment and disposal of organic effluents. The situation leads to public health andenvironmental problem. Therefore, various high rate anaerobic treatments has beenemerged as a variable alternative for the treatment of many industrial and domesticwastewater containing organic wastes. In this study high rate Upflow Anaerobic SludgeBlanket (UASB) reactor has been critically analyzed, discussed and designed as thesolution of above problem. According to that a UASB reactor has been fabricated forlaboratory study. The UASB system appeared to be economically cost effective ascompared to other systems. This paper also focuses on the principle of startup,operational performance, chemical oxygen demand (COD) removal efficiency, methaneproduction rate, and specific methanogenic activity in the UASB reactor. In the presentstudy, reactor was started initially with mixture of molasses and glucose (50% each)solution with organic loading rate (OLR) 0.933 g COD/L day. Thereafter, OLR is beingincreased in steps. After 15 days of startup of reactor, molasses solution was applied. Thetemperature (35e° C), pH (6.8±0.4), and nutrients requirement were maintained. In thisstudy COD: N: P ratio were maintained at 300: IO: l by adding urea for nitrogen andpotassium di-hydrogen phosphate for phosphorus. For a change of OLR up to 13.33gCOD/L day, all above-mentioned parameter were studied. The removal efficiency andgas production rate depend on activity of granules. A typical organic degrading granule iscomposed of micro-colonies of Methanothrix and several syntropic micro -colonies.
污泥反应器中有机废物的生物降解研究
发展中国家的工业化在有机废水的收集、处理和处置方面造成了严重的问题。这种情况导致了公共健康和环境问题。因此,各种高速率厌氧处理已成为处理许多含有机废物的工业和生活废水的可变选择。为解决上述问题,本文对高速率上流式厌氧污泥毯反应器进行了分析、探讨和设计。在此基础上,研制了UASB反应器,并进行了实验研究。与其他系统相比,UASB系统在经济上具有成本效益。本文还重点介绍了UASB反应器的启动原理、运行性能、化学需氧量(COD)去除率、产甲烷率和特定产甲烷活性。本实验以糖蜜和葡萄糖(各占50%)混合溶液为初始反应器,有机负荷率(OLR)为0.933 g COD/L d。此后,OLR正在逐步增加。反应器启动15天后,加入糖蜜溶液。温度(35e°C), pH(6.8±0.4),营养需求维持不变。本研究通过尿素代氮、磷酸二氢钾代磷,将COD: N: P维持在300:IO: 1。当OLR变化至13.33gCOD/L d时,对上述参数进行了研究。除气效率和产气速率取决于颗粒的活性。一个典型的有机降解颗粒是由甲烷菌微菌落和几个共向微菌落组成的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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