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Biological nutrient removal from on-site wastewater treatment systems using a membrane aerated bioreactor

机译:使用膜曝气生物反应器从现场废水处理系统中去除生物营养

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This study aimed to develop a low cost bioreactor process to efficiently removeorganic compounds and nutrients from on-site wastewater treatment systems. Alaboratory-scale anaerobic membrane-aerated biofilm bioreactor (ANMABR) using agas-permeable silicone tubing covered with non-woven fabrics was constructed toevaluate the efficiency of chemical oxygen demand (COD) and nitrogen removal inthe system.After 250 days of continuous reactor operation, the experiment results showedconsistent COD and NH4-N removal efficiencies at 89±6 and 82±5%, respectively.The total nitrogen (TN) removal efficiency was 64±8% with an effluent average totalnitrogen concentration of 11 mg/L. From day 89 to day 120 the biofilm reactorexperienced a shock load running with C/N ratio of 2:1 with influent NH4-N increasedto 150 mg/L. The COD removal efficiency was not affected after the shock load, butNH4-N and TN removal efficiencies were decreased down to 44 and 22%,respectively.This study demonstrated that gas-permeable tubing/membrane could beused to treat wastewater containing low organic and nitrogen loadings from on-sitewastewater treatment systems. Improvement is still needed under the shock loadingconditions for on-site wastewater treatment systems.
机译:这项研究旨在开发一种低成本的生物反应器工艺来有效去除 现场废水处理系统中的有机化合物和养分。一种 实验室规模的厌氧膜曝气生物膜生物反应器(ANMABR)使用 覆盖有无纺布的透气硅胶管用于 评估化学需氧量(COD)和脱氮的效率 系统。 反应器连续运行250天后,实验结果表明 一致的COD和NH4-N去除效率分别为89±6和82±5%。 总氮(TN)去除效率为64±8%,出水平均 氮浓度为11 mg / L。从第89天到第120天,生物膜反应器 经历了C / N比为2:1的冲击负载,而进水NH4-N却增加了 至150 mg / L。冲击负荷后,COD的去除效率没有受到影响,但是 NH4-N和TN的去除效率分别降至44%和22%, 这项研究表明,透气管/膜可能是 用于处理现场有机和氮含量低的废水 废水处理系统。冲击载荷下仍需改进 现场废水处理系统的条件。

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