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Study on a sequencing batch membrane bioreactor for wastewater treatment

机译:测序间歇膜生物反应器处理废水的研究

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This study investigated the effect of MLSS concentration in a sequencing batch membrane bioreactor on COD and nitrogen removal as well as flux. Two values of MLSS (5 g/l and 10 g/l) were investigated in this study. The strength of the feed was varied to achieve a target F/M ratio of 0.5 based on COD. Accordingly, the concentration of COD was determined as 3.5 and 7.0 g/l for the 5 and 10 g/l MLSS targets, respectively. The test results showed that an average COD removal of 98.5% was achievable. However, it was noted that nitrification inhibition occurred. Nitrification inhibition occurred because of two factors, namely high NH4+-N concentration and high DO demand. High NH4+-N in the feed led to the inhibition of nitratation and thus high nitrites are found in the effluent. High DO demand due to high feed COD concentration led to an extended period with low DO levels inside the reactor thus retarding the conversion of NH4+-N. The increase in the MLSS concentration from 5 to 10 g/l led to a decrease in the average flux from 11.1 l/m(2) h to 9.6 l/m(2) h. An increase in aeration, from 2.0 to 8.0 l/min, did not lead to any significant improvement in terms of fouling. [References: 11]
机译:这项研究调查了测序批量膜生物反应器中MLSS浓度对COD和脱氮以及通量的影响。在这项研究中研究了两个MLSS值(5 g / l和10 g / l)。改变进料的强度以达到基于COD为0.5的目标F / M比。因此,对于5和10 g / l MLSS目标,COD的浓度分别确定为3.5和7.0 g / l。测试结果表明,平均COD去除率为98.5%。但是,注意到发生硝化抑制。发生硝化抑制的原因有两个,即高NH4 + -N浓度和高DO需求。进料中的高NH4 + -N导致硝化作用受到抑制,因此在废水中发现了高亚硝酸盐。由于进料COD浓度高而产生的高DO需求导致反应器内部DO含量较低的时间延长,从而阻碍了NH4 + -N的转化。 MLSS浓度从5升至10 g / l导致平均通量从11.1 l / m(2)h降低至9.6 l / m(2)h。曝气量从2.0升/分钟增加到8.0升/分钟,并没有导致结垢方面的任何显着改善。 [参考:11]

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