共查询到19条相似文献,搜索用时 93 毫秒
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化工废水深度处理技术研究进展 总被引:1,自引:0,他引:1
化工废水经二级生化处理后,往往很难达到排放或回用要求,须进行深度处理。综述了化工废水深度处理的技术及特点,并介绍了其最新研究进展。提出了不同处理方法的联合应用将是化工废水深度处理工艺的发展趋势。 相似文献
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为实现电镀废水的深度处理及回用,本文探究了芬顿(Fenton)-活性炭耦合陶瓷膜工艺处理电镀废水生化出水的最佳反应条件,处理效果,运行稳定性,膜污染规律与膜清洗效果。结果表明,当活性炭投加量为40 g/L、换炭量为4%/d、膜通量设置为70 L/(m2·h)时,耦合工艺深度处理效果优异,经30 d运行,出水COD、TOC和浊度分别为14 mg/L、4.5 mg/L和0.04 NTU,去除率均可达到80%以上,满足《城市污水再生利用工业用水水质》(GB/T 19923-2005)标准。活性炭可吸附水中的污染物,增强该工艺对COD的去除效果,还可以有效减缓膜污染,延长膜的运行周期。被污染后的膜,依次经物理清洗和次氯酸钠清洗后,膜通量可恢复至原来的94%。Fenton-活性炭耦合陶瓷膜工艺处理电镀废水生化出水效果优异,具有长期运行稳定性,可作为深度处理工艺,实现电镀废水的深度处理及回用。 相似文献
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芬顿氧化法因其具有较好的有机物降解效果已应用于许多大规模的污水深度处理工程中,近年来发展出以紫外光(UV)/H2O2等方法为代表的类芬顿技术,其基本原理与使用方法均与芬顿技术类似,但光芬顿所需的Fe2+浓度更低,反应不需要很低的pH,运行更加高效、安全和简单。文章通过构建光芬顿反应体系,搭建光芬顿反应装置,以H2O2投加量、亚铁盐投加量、反应pH、光源为反应条件参数,以COD&去除效果为降解性能指标,优化降解反应过程中的工艺参数,验证了光芬顿体系对废水CODCr的去除机理,确定了光芬顿体系的最优反应条件,并研究了降解规律,分析了经济成本,提出了光芬顿体系对印染化工废水深度处理的应用建议。试验中最优反应条件如下:pH值为6,H2O2投加量为400 mg/L,Fe2+投加量为21.0 mg/L。该条件下,经过光芬顿处理,可将二沉池出水的COD& 相似文献
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探讨了陶瓷膜在炼油污水深度处理中的应用,并同时确定了工艺条件,选定了工艺参数,结果表明经二级生化处理的炼油污水经该工艺处理后,完全可达到回用的要求. 相似文献
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对比了臭氧、臭氧催化氧化、臭氧/双氧水和臭氧/双氧水催化氧化4种工艺深度处理化工废水的效果,结果表明,当进水COD和色度分别为95.7 mg/L和90倍时,4种工艺出水的COD去除率分别为23.66%、26.77%、29.24%、32.97%,色度去除率分别为64.44%、64.44%、82.22%、82.22%,催化剂和双氧水均能小幅强化臭氧氧化效果。连续臭氧氧化可使出水COD降至20 mg/L,同时当臭氧投加量为60 mg/L时,4种工艺出水均具有一定的可生化性,满足后序生化工艺的需求。 相似文献
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止咳糖浆制药废水经生物接触氧化一体化废水处理装置处理后,其出水中COD、BOD和氨氮等主要污染物质均不能达标排放。在实验室中采用陶粒过滤陶瓷膜组合对经一体化处理装置处理后的制药废水进行深度处理,在陶粒柱反应器选用粒径为1-2mm的陶粒滤料,陶瓷膜反应器选用孔径为2-3μm陶瓷膜的条件下对水样进行测试。 相似文献
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In areas where tap water has a high salt content, wastewater is not appropriate for reuse in agriculture, particularly for sensitive crops. One alternative is reduction, via desalination, of the brackish character to the secondary effluent. A filtration stage is also required before desalination. On the other hand, used reverse osmosis membranes can be recycled and used as filters in the advanced treatment stage in order to reduce suspended matter contained in the secondary effluent—one advantage being the environmental recovery of solid waste. Used membranes can be treated with strong chemical oxidants to peel off the active separation layer in order to transform them into microfiltration or ultrafiltration elements. Preliminary tests have been carried out with 8″ elements, aimed at comparing membrane performance before and after the peeling process. An index denoted as peeling effectiveness (high flux, high salt passage) is used for comparison. It was soon observed that potassium permanganate was more effective than others, together with sodium hydroxide. Doses around 1000 mg/L KMnO4 provided the best results. It was also concluded that membrane cleaning, done with sodium bisulphite prior to peeling, was better when recirculating the cleaning solution around the membrane rather than soaking it. Next steps in the research will test the actual filtration capability of the peeled membranes in actual wastewater. 相似文献
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Tight ceramic uitrafiltration membranes have been proven to exhibit good rejection performance for reactive dye wastewater at high temperatures because of their high thermal and chemical resistance.However,the application of ceramic membranes for the treatment of cationic dye wastewater is chal-lenging because of their surface charge.In this study,a ceramic membrane is modified by grafting aminosilane (KH-551) to enhance the positive charge of the membrane surface.The rejection perfor-mance of the charged modified ceramic membrane toward the methylene blue solution is significantly improved.The modification substance is bonded to the ceramic membrane surface via covalent bonding,which imparts good thermal stability.The modified ceramic membrane exhibits stable separation perfor-mance toward the methylene blue solution.Overall,this study provides valuable guidance for the adjust-ment of the ceramic membrane surface charge for treating industrial cationic dye wastewater. 相似文献
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《Ceramics International》2023,49(4):5776-5787
Eco-friendly ceramic membranes have been developed from clayey materials mixed with biobased additives (woodworking waste and rice husk) as pore-forming agents. Heated blends of two clayey occurring materials with the biobased additives (up to 20 wt%) were investigated using X-Ray Fluorescence spectrometry (XRF), X-Ray Diffraction (XRD), Thermogravimetric Analysis (TDA-TG), Mercury Porosimetry, Scanning Electron Microscopy/Energy Dispersive Spectroscopy (SEM-EDS) and Filtration tests. The effect of adding the pore-forming agent on the physical and mechanical properties (apparent density, apparent porosity, average pore diameter and compressive Strength) was assessed and the results were interrelated to the microstructural changes. The mineralogical analyzes showed that original minerals together with thermal decomposition products were involved in the neoformation process. SEM observations displayed the appearance of several pores with various shapes, sizes and features corresponding to the neoformed phases (gehlenite and albite) and localized heterogeneous aspects. The experimental filtration tests have clearly shown the elimination of turbidity and suspended matter with the reduction of the chemical/biological oxygen demand and the dye concentration. Thereby, it was confirmed that ceramic membranes intended for filtration with homogenous morphological aspect, good physical properties and high mechanical strength could be manufactured and used in industrial wastewater treatments. 相似文献