工业废水催化湿式氧化处理的研究

采用系列贵金属-半导体氧化物催化剂,在高压釜中250℃液相条件下对焦化厂等工业废水以及由氨、吡啶等组成的模拟废水进行液相氧化试验。结果发现几种催化剂对不同污染物有不同序列的催化氧化活性,其净化作用有各自的选择性。WT-501催化剂对氨和有机污染物均有高活性,焦化废水经WT-501催化氧化处理后’COD、NH_3分別从9302mg/L和5230mg/L降至619mg/L和47mg/L,去除率高达93.2％和99％。     

基于熵权和层次分析法的VOCs处理技术综合评价

针对化工行业所使用的VOCs控制技术,综合考虑了环境、经济、管理以及技术4个一级因素以及13个二级因素对化工企业中常用的VOCs控制技术进行综合评价,建立基于熵权法与层次分析法相结合的模糊综合评价模型,对9种VOCs末端治理技术进行量化分析评价.阐述了备选VOCs的排放控制技术筛选方法、指标体系的构建以及评价方法,最后...     

Adsorption of chlorpyrifos,penconazole and metalaxyl from aqueous solution by modified clays

Sorption of three pesticides (chlorpyrifos, metalaxyl and penconazole) has been measured on a commercial clay montmorillonite and on the same mineral modified with either of two cationic-surfactant micelles. Both micelle–clay complexes, commercial names Cloisite 20A and Cloisite 30B, showed a good capacity to sorb all three pesticides from water, whereas their sorption on the natural montmorillonite was not described by an isotherm. Modelling sorption on both micelle–clay complexes showed that the Freundlich sorption constant (K _F) was higher for chlorpyrifos on Cloisite 20A (K _F = 7.76) than on Cloisite 30B (K _F = 5.91), whereas the sorption of metalaxyl was stronger on Cloisite 30B (K _F = 1.07) than on Cloisite 20A (K _F = 0.57). Moreover the micelle–clay complex Cloisite 20A also showed a good affinity for penconazole, the maximum quantity adsorbed (q _m) of 6.33 mg g^?1 being 45% more than that on Cloisite 30B. Single-batch adsorption of each pesticide onto both micelle–clay complexes was studied using the Freundlich isotherm for chlorpyrifos and metalaxyl and the Langmuir isotherm for penconazole. The Cloisite 20A micelle–clay complex was predicted to require 23% less adsorbent to treat certain volumes of wastewater containing 30 mg L^?1 chlorpyrifos, 43% more to treat metalaxyl similarly and 57% less to treat penconazole compared with Cloisite 30B.     

Treating solid dairy manure using microwave-enhanced advanced oxidation process

The microwave enhanced advanced oxidation process (MW/H₂O₂-AOP) was used to treat separated solid dairy manure for nutrient release and solids reduction. The MW/H₂O₂-AOP was conducted at a microwave temperature of 120°C for 10 minutes, and at three pH conditions of 3.5, 7.3 and 12. The hydrogen peroxide dosage at approximately 2 mL per 1% TS for a 30 mL sample was used in this study, reflecting a range of 0.53–0.75 g H₂O₂/g dry sludge. The results indicated that substantial quantities of nutrients could be released into the solution at pH of 3.5. However, at neutral and basic conditions only volatile fatty acids and soluble chemical oxygen demand could be released. The analyses on orthophosphate, soluble chemical oxygen demands and volatile fatty acids were re-examined for dairy manure. It was found that the orthophosphate concentration for untreated samples at a higher % total solids (TS) was suppressed and lesser than actual. To overcome this difficulty, the initial orthophosphate concentration had to be measured at 0.5% TS.     

Adsorption of simazine on zeolite H-Y and sol–gel technique manufactured porous silica: A comparative study in model and natural waters

In this work, we studied the removal of simazine from both a model and well water by adsorption on two different adsorbents: zeolite H-Y and a porous silica made in the laboratory by using the sol–gel technique. The pH dependence of the adsorption process and the isotherms and pseudo-isotherms of adsorption were studied. Moreover, an iterative process of simazine removal from both the model and well water, which allowed us to bring the residual simazine concentration below the maximum concentration (0.05 mg L^?1) of agrochemicals in wastewater to be released in surface waters or in sink allowed by Italian laws, was proposed. The results obtained were very interesting and the conclusions drawn from them partly differed from what could reasonably be expected.     

Landfill leachate treatment methods: A review

Landfilling of municipal waste is still a major issue of the waste management system in Europe. The generated leachate must be appropriately treated before being discharged into the environment. Technologies meant for leachate treatment can be classified as follows (i) biological methods, (ii) chemical and physical methods. Here we review briefly the main processes currently used for the landfill leachates treatments.     

柴油低温临界吸收法回收装车挥发油气

研究了采用柴油低温临界吸收法回收装车挥发油气的效果。实验结果表明：按装车挥发油气中的总烃体积分数为20.88%、装车挥发油气流量为280 m³/h、年运行时间为2 668 h计,装置年回收油气量为291 t,装置年最大运行功率为206.770 MW,装置投资回收期为3 a;处理后净化气中的总烃体积分数为1.24%,排放质量浓度低于25 g/m³,油气回收率达95%。处理后净化气满足GB 20950—2007《储油库大气污染物排放标准》,取得了较好的环保效益和经济效益。     

含氨氮催化剂生产废水的处理

采用加入淀粉的短程硝化-反硝化一体化技术处理低碳含NH3-N催化剂废水。通过中试确定了适宜的工艺参数,并在工业化装置上进行了验证。试验结果表明：在DO为0.5 mg/L左右、淀粉加入量为0.25 kg/ m3、HRT=30 h的条件下,短程硝化-反硝化一体化技术具有较好的处理效果,NH3-N去除率大于97%,且具有较强的抗冲击负荷的能力; 出水的COD<100 mg/L,ρ（NH3-N）<10 mg/L,达到GB 8978—1996《污水综合排放标准》的一级排放标准。工业化装置的运行费用以NH3-N计为2.3 元/kg、以废水计为4.6 元/t。该法适用于中低浓度（ρ（NH3-N）<300 mg/L）废水的处理。     

基于AHP的密闭环境空气质量评价模型及其应用

针对指数法在评价密闭环境空气质量中存在评价因素单一,不能反映多种污染物对空气环境质量的综合影响等缺点,结合模糊数学的原理与方法,对密闭环境空气质量进行评价。采用层次分析法赋权,按最大隶属原则,通过模糊数学模型对某密闭环境空气质量进行综合评价,评价结果较科学地反映了空气质量的真实状况。     

基于核心企业视角的虚拟生态工业园构建分析

虚拟生态工业园(VEIP)是一种基于循环经济的新型的大循环生态工业组织形式,是对实体生态工业园的补充和扩展.而核心企业作为VEIP的组建者,是整个园区日常运营的信息指挥中枢,对VEIP的成功运营至关重要.分析了核心企业的内涵和应具备的特质,然后从核心企业的视角出发,给出了核心企业构建VEIP的一般流程,并阐述了核心企业在VEIP构建过程中的主要职能.