首页> 外文期刊>Journal of environmental engineering and managent >ELECTRO-FENTON-BASED TREATMENTS OF REAL EFFLUENTS FROM TANNING PROCESSES AND LANDFILLS
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ELECTRO-FENTON-BASED TREATMENTS OF REAL EFFLUENTS FROM TANNING PROCESSES AND LANDFILLS

机译:制革过程和填埋料中基于电子芬顿的实际废水处理

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摘要

Leather industry uses high quantities of water, from 50 to 200 m~3 d~(-1) and tanning processes use large quantities of tannin-based organic compounds, which with all the protein, lipids, greases and hairs, constitute high amounts of COD (chemical oxygen demand) and BOD (biological oxygen demand) with many biorefractory compounds in the tanning effluents. Effective treatment with recycling option of such large quantities of technological waters would: 1) reduce the costs of the entire tanning process (as for that of water consumption and that of salt expenses), 2) allow to easily depurate the issuing waters with lower costs, and 3) eliminate progressively the negative environmental impact of the final effluent discharge into rivers by reducing considerably (or eliminating) the remaining COD and the quantities of sludge at the end of the treatment process.rnDepuration sludges are usually stocked in specially conceived landfills. Leachate from such landfills contains also high quantities of contaminants, COD from 5000-15000 ppm, and requires further treatment. Periodical recirculation of the leachate is done, which, in fact, does not always suffer subsequent treatment.rnThe main process presented in this work, H_2O_2-assisted electroprecipitation (AEP) with sacrificial Fe anode coupled with Ti(Pt) cathode, combines physico-chemical aspects of the treatment of water effluents with electro-Fenton(EF)-based electrochemical oxidation and partial coagulation/precipitation of the remaining compounds. The COD removal is 90% in 8 h for the desalting wastewater and in the range 60-80% in 6 h for the leachate during AEP treatment. EF and photoelectron-Fenton on boron doped diamond (BDD) anode coupled with O_2-diffusion cathode also allow high degradation efficiency (75-80%), limited by oxalate-complexes formation and the presence of suspended solids. BDD anodic oxidation achieves 99% destruction of COD in a longer time, more than 20 h. AEP treatment, alone or in combination with complementary treatment, allows complete COD removal from the effluents. The AEP-technology is suitable to industrial application specially for the recycling of tanning effluents and landfill leachate.
机译:皮革工业使用大量的水,从50到200 m〜3 d〜(-1),鞣制过程中使用大量的单宁类有机化合物,这些化合物与所有蛋白质,脂质,油脂和头发一起构成大量的制革废水中的化学需氧量(COD)和生物需氧量(BOD)以及许多生物难降解化合物。使用如此大量的技术水进行再循环选择的有效处理方法将:1)降低整个制革过程的成本(如水消耗和盐分费用的成本),2)允许以较低的成本轻松净化出水3)通过在处理过程结束时显着减少(或消除)残留的COD和污泥量,逐步消除最终废水排入河流的负面环境影响。净化污泥通常存放在专门设计的垃圾填埋场中。来自此类垃圾填埋场的渗滤液还含有大量污染物,COD为5000-15000 ppm,需要进一步处理。定期进行渗滤液的再循环,实际上并不总是进行后续处理。这项工作中介绍的主要过程是H_2O_2辅助电沉淀(AEP)和牺牲Fe阳极与Ti(Pt)阴极结合,将物理基于基于Fenton(EF)的电化学氧化和剩余化合物的部分凝结/沉淀处理废水的化学方面。在AEP处理过程中,脱盐废水在8小时内的COD去除率为90%,渗滤液在6小时内的COD去除率为6-60%至80%。 EF和掺硼金刚石(BDD)阳极上的光电子Fenton与O_2扩散阴极耦合也可实现高降解效率(75-80%),受草酸盐复合物形成和悬浮固体的存在限制。 BDD阳极氧化可在20小时以上的较长时间内实现99%的COD破坏。单独或与辅助处理结合使用AEP处理,可从废水中完全去除COD。 AEP技术特别适合工业应用,用于鞣革废水和垃圾填埋场渗滤液的回收。

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