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Desalination of Mixed Tannery Effluent with Membrane Bioreactor and Reverse Osmosis Treatment

机译:膜生物反应器处理混合制革废水的脱盐及反渗透处理。

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摘要

A limiting factor for the reuse and recycling of treated tannery wastewater for irrigation and other uses is the high salt content,which persists even after conventional treatment.Reverse osmosis(RO)membrane treatment has been shown to significantly reduce the salt contents of tannery effluents.However,the high organic content of tannery effluent leads to rapid scaling and biofouling of RO membranes with a consequent reduction in flux rates and performance.Membrane bioreactors(MBR)have been shown to be highly effective in the removal of organic pollutants and suspended solids from tannery effluent.This research investigated the use of a combined MBR and RO treatment process to treat tannery effluents to an acceptable level for irrigation purposes.The MBR was operated at 17-20 h retention time,at a F/M ratio of 0.52 kg COD centre dot kg SS~(-1)centre dot day~(-1)and a volumetric loading rate of 3.28 kg COD centre dot m~(-3)centre dot day~(-1).This treatment reduced the COD,BOD,and ammonia concentrations of the effluent by 90-100%.The MBR was shown to be an excellent pretreatment prior to RO technology,due to the high removal efficiency of organic compounds and suspended solids,with average concentrations of 344 mg centre dot L~(-1)COD and 20 mg centre dot L~(-1)BOD achieved in the permeate.RO treatment reduced the salt content of the MBR permeate by up to 97.1%.The results of the research demonstrated that the MBR system developed was appropriate for the treatment of tannery effluents and,in combination with the RO treatment,reduced the salt content to acceptable levels for irrigation.The MBR pretreatment reduced bio-fouling and scaling of subsequent RO treatment and improved the overall performance of the RO unit.It is believed that this is the first investigation of a combined MBR and RO treatment for tannery effluents.This research provided data for an outline design of a full-scale MBR and RO plant with a treatment capacity of 5000 m~3 per day for mixed tannery effluents.
机译:高处理后的制革废水用于灌溉和其他用途的再利用和再循环的限制因素是高盐含量,即使在常规处理之后仍会保持较高的盐含量。反渗透(RO)膜处理已显示出可大大降低制革废水的含盐量。然而,制革厂废水中有机物含量高导致反渗透膜快速结垢和生物结垢,从而降低了通量率和性能。膜生物反应器(MBR)在去除有机污染物和悬浮固体方面非常有效。制革厂废水。本研究调查了MBR和RO联合处理工艺如何将制革厂废水处理至可接受水平以用于灌溉目的.MBR在保留时间17-20小时下运行,F / M比为0.52 kg COD中心点千克SS〜(-1)中心点日〜(-1)和3.28 kg COD的体积加载速率中心点m〜(-3)中心点日〜(-1)。该处理降低了COD,BOD和废水的浓度为90-100%。由于有机化合物和悬浮固体的去除效率高,MBR在RO技术之前是一种很好的预处理方法,平均浓度为344 mg中心点L〜(- 1)渗透物中获得了COD和20 mg中心点L〜(-1)BOD.RO处理使MBR渗透物中的盐含量降低了97.1%,研究结果表明开发的MBR系统适用于制革厂废水的处理以及与RO处理相结合,将盐含量降低到可接受的灌溉水平.MBR预处理减少了后续RO处理的生物结垢和结垢,并提高了RO装置的整体性能。这是对MBR和RO联合处理制革厂废水的首次研究。这项研究为规模为每天5000 m〜3的混合制革厂处理能力的MBR和RO大型装置的总体设计提供了数据。流出物。

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  • 来源
    《Environmental Science & Technology》 |2005年第21期|p.8505-8511|共7页
  • 作者单位

    W2O Environment,Queen's Park,58 Cecil Road,NN2 6PQ,Northampton,United Kingdom,AGBAR,Aguas de Barcelona,Division Agua y Sanamiento,Paseig de Sant Joan 39-43,8009 Barcelona,Spain,Departamiento de Ingenieria Quimica,Universidad de Murcia,30007 Espinardo;

    W2O Environment,Queen's Park,58 Cecil Road,NN2 6PQ,Northampton,United Kingdom,AGBAR,Aguas de Barcelona,Division Agua y Sanamiento,Paseig de Sant Joan 39-43,8009 Barcelona,Spain,Departamiento de Ingenieria Quimica,Universidad de Murcia,30007 Espinardo;

    W2O Environment,Queen's Park,58 Cecil Road,NN2 6PQ,Northampton,United Kingdom,AGBAR,Aguas de Barcelona,Division Agua y Sanamiento,Paseig de Sant Joan 39-43,8009 Barcelona,Spain,Departamiento de Ingenieria Quimica,Universidad de Murcia,30007 Espinardo;

    W2O Environment,Queen's Park,58 Cecil Road,NN2 6PQ,Northampton,United Kingdom,AGBAR,Aguas de Barcelona,Division Agua y Sanamiento,Paseig de Sant Joan 39-43,8009 Barcelona,Spain,Departamiento de Ingenieria Quimica,Universidad de Murcia,30007 Espinardo;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 环境化学;
  • 关键词

  • 入库时间 2022-08-17 14:07:58

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