无机高分子絮凝剂聚合硅酸铝铁的研究

以ALCL3，FeCl3，Na2SiO3和盐酸为原料，采用NaOH作为碱化聚合剂，合成了具有不同碱化度（B），不同Al/Fe/Si摩尔比的铝铁硅共聚物（简称PAFSC），通过PH滴定法测定分析了铝、铁在其水解共聚合过程中PH值的变化，然后通过透射电镜和混凝实验对共聚物的晶形貌像和絮凝作用进行了研究，通过对模拟具有色悬浊水样的絮凝实验，并与现有的其它无机絮凝剂作比较后可以看出：在同样投加量情况下，PAFSC处理的水具有更低的剩余浊度和色度。     

淀粉废水处理工艺选择

针对淀粉废水的特性 ,通过大量实验 ,提出合理的处理工艺 ,在实际运行中取得了较好的处理效果 ,节省了占地和建设投资     

焦炭和废铁屑微电解预处理垃圾渗滤液的研究

研究表明,废铁屑和焦炭微电解是预处理垃圾渗滤液的一种有效方法,可去除垃圾渗滤液COD、色度和腐殖酸等污染物质,改善其可生化性、降低负荷,为后续生化处理创造良好的条件.通过静态正交实验确定废铁屑和焦炭最佳投加体积比为1∶3;最佳反应pH值为4;动态实验中,反应时间为1 h时,COD和色度去除率分别高达68%和91%;BOD/COD从0.3提高到0.5左右.     

组合式生物膜法处理炼油废水的研究

针对炼油废水成分复杂、有毒物质含量高和可生化性差的特点,采用组合式生物膜法进行处理.试验结果表明,该工艺对COD、NH3-N和挥发酚(Ar-OH)具有较好的去除效果,去除率分别为92.6%、96.5%和98.1%,达到《污水综合排放标准》(GB 8978-1996)一级标准.     

厌氧-好氧生化处理淀粉废水的工程应用

通过邳州市奋达淀粉有限公司的工程实例,介绍了厌氧-好氧生化处理工艺在处理淀粉生产废水中的应用.该工艺具有处理设施运行稳定,处理效果好的优点,系统出水水质满足《污水排放标准》一级标准要求.     

印染工业废水处理工程设计要点

结合印染工业废水处理工程现状，提出应重视印染废水处理工程的工艺设汁，分析讨论了在印染工业废水处理工程设汁中要引起注意的三个方面问题。     

臭氧在污泥减量技术中的应用

大量的剩余污泥已成为国内外污水处理行业亟待解决的问题,因此各种物理、化学和生物方法被应用到污泥处理中,臭氧以其独特的性质从一开始应用就备受青睐.详细地说明了臭氧在污泥减量技术中应用的背景及原理,重点介绍了臭氧对污泥性质的影响,并分别从臭氧氧化技术与传统活性污泥法组合、与AO工艺组合、与膜生物反应器(MBR)组合、与磷回收工艺组合、与SBR工艺组合等角度分析了臭氧在污泥减量技术中的应用与现状、目前存在的问题及未来的发展方向.     

Decolorization and biodegradation of dye wastewaters by a facultative-aerobic process

BACKGROUND: Dye wastewater is one of the main pollution sources of water bodies in China. Conventional biological processes are relatively ineffective for color removal, the development of alternative treatment methods will become important. Our subjective was that of introducing a new biotreatment technology which combined a facultative biofilm reactor (FBR) with an aerobic reactor (AR) to treat a dye wastewater. The efficiencies of color and chemical oxygen demand (COD) removal and the mechanism of dye degradation were investigated. METHODS: The anthraquinone acid dye (acid blue BRLL) concentration, organic loading rate (OLR) and hydraulic retention time (HRT) were varied in the experiments to evaluate the treatment efficiency and process stability. The biodegradation products were detected by infrared (IR) and high performance liquid chromatography and mass spectrometry (HPLC-MS). RESULTS AND DISCUSSION: The results demonstrated that the facultative biofilm process was more effective for decolorization than the anaerobic stage of an anaerobic-aerobic process. Most color removal occurred in the facultative reaction (maximum to 88.5%) and the BOD (biochemical oxygen demand): COD of the FBR effluent increased by 82.2%, thus improving the biodegradability of dyes for further aerobic treatment. The dye concentration, OLR and HRT will be the factors affecting decolorization. Color removal efficiency falls as the influent dye concentration increases, but rises with increased HRT. The infrared and HPLC-MS analyses of the effluents of FBR and AR reveal that the dye parent compound was degraded in each reactor during the process. CONCLUSION: The Facultative-aerobic (F-A) system can effectively remove both color and COD from the dye wastewater. The FBR played an essential role in the process. The average overall color and COD in the system were removed by more than 93.9% and 97.1%, respectively, at an OLR of 1.1 kg COD m(-3) d(-1) and at the HRT of 18-20 hours in the FBR and 4-5 hours in the AR. The color removal mechanism in each reactor was not only a sort of biosorption on the floc materials, but even more an effect of biodegradation, especially in the facultative process. Recommendation and Outlook. In applying the F-A system to treat a dye wastewater, the control of facultative processes and the set up of appropriate operation conditions appear to be critical factors. Also, it is suggested a moderate COD loading rate and about a 24-hour HRT will favor the F-A system.     

铜酞菁生产中的三废综合治理及其资源化探讨

通过某铜酞菁化工生产企业三废治理及其资源化工艺改进的实践，总结出了一套行之有效的利用酸化工艺废酸的资源化新方法，不但从中回收了高价值的铜泥；同时利用废酸吸收生产工艺中的高含氨尾气，生产硫酸铵，达到了以废治废的目的，整个治理工艺符合循环经济的理念。通过该回收工艺的改进，使上述三废不再进入污水处理系统，从而解决了传统铜酞菁生产废水的高酸度、高盐分、高含氨、高难处理的矛盾，使铜酞菁三废处理易于实行。     

炼油厂轻污染水回用试验研究

针对某炼油厂轻污染废水水质情况，选用了BAF（生物曝气滤池）工艺＋SF（砂滤）工艺对该废水进行净化处理。通过试验研究，得到了BAF工艺合适的运行参数，取得了满意的试验结果。经BAF工艺处理后，出水COD和油平均浓度分别为9.78mg／L和0.24mg／L，再经SF工艺进一步去除SS后，出水SS平均浓度为3．8mg／L，系统处理出水完全达到工业回用水水质要求。试验证明：BAF工艺是一种高效的处理方法，适合炼油厂轻污染水的净化处理。