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Polyurethane rotating disc system for post-treatment of anaerobically pre-treated sewage

机译:厌氧预处理污水后处理的聚氨酯转盘系统

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摘要

The performance of polyurethane rotating discs (RBC-1) versus polystyrene rotating discs (RBC-2) for the treatment of an up-flow anaerobic sludge blanket (UASB) reactor effluent fed with domestic wastewater was investigated. Both RBC units were operated at the same organic loading rate (OLR) of 10.5 gCOD/m~2 d. and a hydraulic retention time (HRT) of 2.5 h. The residual values of COD fractions (COD_(suspended, COD_(colloidal) and COD_(soluble)) in the treated effluent of RBC-1 and RBC-2 were similar. However, the removal efficiency of ammonia in the RBC-1 (87 ± 4%) was significantly higher than that found for RBC-2 i.e. 24 ± 6%. Moreover, RBC-1 achieved a substantial removal efficiency of 99.0 ± 1% for Escherichia coli (E coli), while RBC-2 removed 91.2 ± 0.3%. Based on these results, optimization of RBC-1 treating UASB reactor effluent was extensively performed. The RBC-1 was operated at an OLR's of 4.0,11 and 23 gCOD/ m~2 d. The results obtained showed that increasing the OLR from 11.0 to 23.0 gCOD/m~2 d and decreasing the HRT from 2.5 to 1.25 h significantly declined the effluent quality of COD_(total) and ammonia. However, the residual values of CODtotai and ammonia remained unaffected when increasing the OLR from 4.0 to 11.0 gCOD/m~2 d and by decreasing the HRT from 5 to 2.5 h. Bacteriological examination showed that the mean residual count of E. coli remained at a level of 10~4/100 ml, in the effluent of RBC-1 independent on the imposed HRT. Accordingly, it is recommended to operate RBC-1 for treatment of anaerobically pre-treated sewage at an OLR of 11 gCOD/m~2 d and an HRT of 2.5 h.rnA feed-less (ammonia limitation) period of 9.0 days followed by 9.0 days feeding with high OLR of 26 gCOD/m~2 d. (raw sewage) was investigated to elaborate, if the nitrifiers of the RBC-1 are capable to convert ammonia to nitrate after totally 18 days when retuning back to the normal operating conditions. The results of the experiment clearly show a strong and immediate detrimental effect of imposing high OLR of 26 gCOD/m~2 d on the nitrification process in the nitrifying RBC unit. However, after returning back to the original OLR of 10.6 gCOD/m~2 d, the nitrification efficiency in the RBC unit was recovered within 2-3 days.
机译:研究了聚氨酯旋转圆盘(RBC-1)与聚苯乙烯旋转圆盘(RBC-2)在处理生活污水进水的厌氧污泥层(UASB)反应器废水中的性能。两个RBC单元均以10.5 gCOD / m〜2 d的相同有机负荷速率(OLR)运行。水力停留时间(HRT)为2.5小时。在RBC-1和RBC-2处理后的废水中,COD分数(悬浮的,COD_(胶体的)和COD_(可溶的)的残留值相似,但是,RBC-1中氨的去除效率(87) ±4%)显着高于RBC-2的24±6%;此外,RBC-1对大肠杆菌的去除效率为99.0±1%,而RBC-2的去除效率为91.2± 0.3%。基于这些结果,广泛地进行了RBC-1处理UASB反应器废水的优化,RBC-1在4.0、11和23 gCOD / m〜2 d的OLR下运行。 OLR从11.0 gCOD / m〜2 d降至23.0 gCOD / m〜2 d,HRT从2.5 h降至1.25 h显着降低了COD_(total)和氨的出水质量,但当将OLR从4.0增加时,CODtotai和氨的残留值保持不变。降低至11.0 gCOD / m〜2 d,并将HRT从5 h降低至2.5 h。细菌学检查显示平均残留在不依赖于HRT的情况下,RBC-1流出物中的大肠杆菌计数保持在10〜4/100 ml的水平。因此,建议操作RBC-1来处理厌氧预处理的污水,其OLR为11 gCOD / m〜2 d,HRT为2.5 h.rnA的无饲料(氨限制)期为9.0天,随后饲喂9.0天,高OLR为26 gCOD / m〜2 d。如果将RBC-1的硝化器恢复到正常操作条件后,在总共18天后能够将氨转化为硝酸盐,则对“原污水”进行了详细研究。实验结果清楚地表明,对硝化RBC装置的硝化过程施加26 gCOD / m〜2 d的高OLR会立即产生强烈而有害的影响。然而,在回到原始的10.6 gCOD / m〜2 d的OLR后,RBC装置的硝化效率在2-3天内恢复。

著录项

  • 来源
    《Journal of Environmental Management》 |2010年第5期|p.1183-1192|共10页
  • 作者

    A. Tawfik; A. Klapwijk;

  • 作者单位

    National Research Center, Water Pollution Research Dept. El-tahrir St., Dokki, P.O. Box 12622, Cairo, Egypt;

    rnWageningen University & Research Center, Agrotechnology and Food Sciences Department, Sub-department of Environmental Technology, P.O. Box 8129, 6700EV, Wageningen, The Netherlands;

  • 收录信息 美国《科学引文索引》(SCI);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    UASB; post-treatment; RBC; polyurethane; COD; nitrification; E. coli;

    机译:UASB;后处理红细胞;聚氨酯化学需氧量硝化作用大肠杆菌;
  • 入库时间 2022-08-17 13:35:31

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