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Performance of HUASB reactor for treating paper & Pulp wastewater using Effective Microorganism(EM)

机译:HUASB反应器利用有效微生物(EM)处理纸浆和纸浆废水的性能

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Pulp and paper industry is one of the most polluting industries all over the world that uses significant amount of fresh water and produces substantial amount of solid and liquid waste. Wastewater from this industry is potentially polluting nature and before discharge into natural course, it is mandatory to adhere to the discharge norms. Anaerobic treatment of paper processing wastewater has a distinct advantage of recovery of inherent energy in the form of methane gas with less sludge production. A hybrid reactor (HUASB) that capitalizes on the positive features of anaerobic filter (AF) and up-flow anaerobic sludge blanket (UASB). The main objective of the thesis is to find out the performance efficiency of the hybrid up-flow anaerobic sludge blanket (HUASB) reactor for treatment of pulp & paper mill wastewater using Effective Microorganism(EM). In this study, a labscale HUASB reactor of 9.68 litres and an effective volume of 7.88 L had been used at ambient temperature with PVC packing materials in the top one third of the reactor. The reactor was initially filled with 2L of cow dung and 2L with seed sludge and remaining with pulp and paper mill wastewater. Start-up was successfully carried out for 130 days and a steady state condition has attained. The reactor was start with an initial influent COD of 750 mg/l, VFA of 65 mg/L with an Organic Loading rate (OLR) of 0.75 kg COD/m3.d and Hydraulic Retention Time( HRT) of 24 hours(hrs) and gradually OLR increased. In order to optimize HRT, various HRT were adapted from 24 hrs to 8 hrs and the maximum effluent COD removal of 83% was observed at a HRT of 12 hours with a gas production of 1.162 L/ L reactor volume/day and methane gas content observed as 71% with a rate of 0.28 m3/kg COD removed. After start up, treatment performance using Activated EM and higher OLR has been loaded for attaining steady state by increasing the influent COD concentration adopting HRT 12 hrs for a period of another 130 days. The maximum effluent COD removal efficiency of 92%, achieved with an OLR of 9.00 Kg COD/m3.day, with gas production of 3.2 L/L.day with 72% methane content and production rate of 0.29 m3/kg COD removed.
机译:纸浆和造纸工业是世界上污染最严重的行业之一,它消耗大量的淡水,并产生大量的固体和液体废物。该行业的废水可能会污染自然环境,在排放到自然过程之前,必须遵守排放标准。造纸废水的厌氧处理具有显着的优势,即以甲烷气体的形式回收固有能量,而产生的污泥较少。利用厌氧滤池(AF)和上流厌氧污泥层(UASB)的积极特性的混合反应堆(HUASB)。本文的主要目的是找出使用高效微生物(EM)处理混合向上流厌氧污泥床(HUASB)反应器处理纸浆和造纸厂废水的性能效率。在这项研究中,已在环境温度下使用9.68升的实验室规模HUASB反应器和有效容积为7.88 L,反应器顶部三分之一使用PVC填充材料。最初将2L牛粪和2L种子污泥装满反应器,并剩余纸浆和造纸厂废水。成功启动了130天,并达到了稳定状态。该反应器的初始进水COD为750 mg / l,VFA为65 mg / L,有机负荷率(OLR)为0.75 kg COD / m3.d,水力停留时间(HRT)为24小时(小时)。并逐渐增加了OLR。为了优化HRT,将各种HRT从24小时调整为8小时,在12小时的HRT观察到最大废水COD去除率为83%,气体产量为1.162 L / L反应器体积/天和甲烷气体含量去除率为0.28立方米/千克,观察到为71%。启动后,采用HRT 12小时增加进水COD浓度(使用HEM 12小时再保持130天),从而获得了使用活化EM和更高OLR的治疗性能以达到稳定状态的目的。 OLR为9.00 Kg COD / m3.day时,最大出水COD去除效率为92%,产气量为3.2 L / L.day,甲烷含量为72%,去除率为0.29 m3 / kg COD。

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