首页> 外文会议>Power and Energy Engineering Conference (APPEEC), 2010 >Post-treatment of Coal Gasification Wastewater Using a Moving Bed Biofilm Reactor in Present of Methanol
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Post-treatment of Coal Gasification Wastewater Using a Moving Bed Biofilm Reactor in Present of Methanol

机译:在甲醇存在下使用移动床生物膜反应器对煤气化废水进行后处理

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Laboratory scale moving bed biofilm reactor (MBBR) was used to treat effluent from post-denitriflcation process in full-scale coal gasification wastewater treatment plant. Methanol was added into the effluent from post-denitriflcation to investigate the effect of surplus methanol on reactor performance. The average effluent COD, NH4-N and NO2-N concentrations were 145.14, 11.88 and 0.22 mg/L for blank reactor (without adding methanol), respectively. The performance of MBBR was little affected when the surplus methanol concentration was 54 mg/L and after acclimation the average effluent COD, NH4-N and NO2-N concentrations were 137.35, 15.2 and 0.44 mg/L, respectively. With the increase of methanol concentration from 90 to 180 mg/L, the effluent NH4-N concentrations increased from 20.31 to 29.18 mg/L. The results indicated that surplus methanol concentration in the effluent from post-denitrification must be controlled below 54 mg/L to avoid negative effect on the post-treatment process.
机译:实验室规模的移动床生物膜反应器(MBBR)被用于处理大型煤气化废水处理厂中的反硝化过程后的废水。在反硝化后的废水中加入甲醇,以研究剩余甲醇对反应器性能的影响。空白反应器(不添加甲醇)的平均出水COD,NH 4 -N和NO 2 -N浓度分别为145.14、11.88和0.22 mg / L。当过剩甲醇浓度为54 mg / L时,MBBR的性能受到的影响很小;经过驯化后,平均出水COD,NH 4 -N和NO 2 -N的浓度为MBBR的性能。分别为137.35、15.2和0.44 mg / L。随着甲醇浓度从90 mg / L增加到180 mg / L,出水NH 4 -N浓度从20.31 mg / L增加到29.18 mg / L。结果表明,必须将反硝化后废水中多余的甲醇浓度控制在54 mg / L以下,以避免对后处理过程产生负面影响。

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