Enhancing biological removal of nitrogen from wastewater in activated sludge process

Q2 Engineering
Taha Sharkawy, Hesham Abdel Halim, Mahmoud M. Abd Elazeem, Mohamed Abdel Moneim Haikal, E. Rozaik
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引用次数: 0

Abstract

ABSTRACT The removal of total nitrogen from wastewater has become a worldwide emerging concern because the compounds of nitrogen, ammonium, nitrite, also nitrate are toxic to aquatic species and causes eutrophication in natural water environments; although activated sludge technology is old, but until now it is effective in the removal of nitrogen compounds. To enhance the removal of nitrogen compounds, a modified process including the usage of internal mixed liquor recycling pump (IMLR), with variable rates starting gradually from one to fifth of influent flow. A Pilot plant consists of three tanks, the first and the second tanks are rectangular, and the third is circular with a conical bottom which acts as a final sedimentation tank. The experiments divided into four phases; phase (1) consists of (A.T), anoxic T. and finally, sedimentation tank with using (IMLLR) rates from (1-4) influent flow, phase (2) as phase (1) but without using (IMLR), phase (3) consists of anoxic tank, (A.T) and final sedimentation tank with using (IMLLR) rates from (1-5) influent flow, finally phase (4) as phase (3) but without using (IMLLR), the average DO in (A.T) about 2.5mg/l, the temperature ranged from (18 – 21), PH ranged from (6.5 – 8). Total nitrogen removal was 61.5% in phase one, 27% in phase two, 64.5% in phase three, and 27% in phase four. The most effective removal of nitrogen in phase (3), with rateQIMLR = 2QINFachieve 64.5% of total nitrogen removal, then in phase (1) with rate QIMLR=3QINF. Achieve 62.39% of total nitrogen removal.
活性污泥法提高废水中氮的生物去除效果
摘要废水中氮、铵、亚硝酸盐和硝酸盐等化合物对水生生物具有毒性,并引起水体富营养化,因此去除废水中的总氮已成为全球关注的热点;活性污泥技术虽然历史悠久,但迄今为止在去除含氮化合物方面是有效的。为了加强对氮化合物的去除,采用了一种改进的工艺,包括使用内部混合液回收泵(IMLR),从进水流量的1 / 5逐渐开始可变速率。一个试验工厂由三个水箱组成,第一个和第二个水箱是矩形的,第三个是圆形的,底部是锥形的,作为最终沉淀池。实验分为四个阶段;阶段(1)由(A.T),缺氧t组成,最后是沉淀池,使用(1-4)的流量(IMLLR)速率,阶段(2)作为阶段(1),但不使用(IMLR),阶段(3)包括缺氧池,(A.T)和最终沉淀池,使用(1-5)的流量(IMLLR)速率,最后阶段(4)作为阶段(3),但不使用(IMLLR), (A.T)的平均DO约为2.5mg/l,温度范围为(18 - 21)。PH范围为(6.5 - 8)。第一阶段的总氮去除率为61.5%,第二阶段为27%,第三阶段为64.5%,第四阶段为27%。相(3)的脱氮效果最好,其速率QIMLR= 2qinf,达到总氮去除率的64.5%;相(1)次之,其速率QIMLR=3QINF。达到总氮去除率62.39%。
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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来源期刊
CiteScore
2.00
自引率
0.00%
发文量
9
审稿时长
52 weeks
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