超滤法处理清洗乳化液废水的应用研究

采用自制超滤膜设备对上海拖拉机内燃机公司油嘴油泵 清洗乳化废水进行了实验室试验，和近一年的生产性应用，结果表明，清洗乳化液废水经超滤处理，ＣＯＤｃｒ去除率为８５％－９１％，油的去除率为９９．４％－９９．９％，出水添加适量新清洗剂后可以回用于生产。     

化工生产中的清洁工艺

简述了清洁生产产生的背景及其重要意义，从改进工艺（聚乙烯醇生产工艺改革），改变生产原料（以乙烯取代乙炔作为合成有机中间体的原料），应用生物技术（两步发酵法生产维生素Ｃ）和改变反应设备（离子膜法生产氢氧化钠）等４个方面说明清洁工艺在化工生产领域取得的实际成效。     

膜分离稀土废水预处理中钙镁去除的研究进展

稀土废水成分复杂,硬度高,利用膜法处理时,进膜之前必须进行预处理.介绍了降低稀土废水硬度传统的和新型的方法.经过分析得出,根据具体水质情况,选择适当的互补处理方法,稀土废水完全可达到膜分离装置进水水质要求.     

膜电除尘器-静电除尘新技术

膜电除尘器是将炭纤维或硅纤维编织膜作为集尘极的新式电除尘器,它克服了传统电除尘器存在的一些缺点,进一步提高了除尘效率,降低了电除尘器的造价,同时能去除粉尘中的酸性盐.介绍了膜电除尘器的结构、特点及除尘性能,并指出了进一步研究的方向.     

好氧生物处理污染水体的供氧技术

针对好氧生物处理污染水体需要充足的溶解氧，阐述了氧传递原理、传统供氧技术（机械供氧，鼓风供氧、氧载体供氧）和新型供氧技术（射流曝气供氧、膜供氧）。指出氧载体供氧和膜供氧技术具有广阔的应用前景。从材料，工艺及应用等方面详细介绍了膜供氧技术的研究进展，并对其发展前景进行了展望。     

膜—生物反应器特性影响因素研究

通过对外压管式膜组件与曝气池构成的好氧膜生物反应器的研究，分别考究膜组件的操作压力，膜面流速以及活性污泥混合液的污泥浓度，溶解性有机特的含量和温度等对膜通量的影响。     

A review of removal technology for antimony in aqueous solution

Antimony (Sb) and its compounds, toxic metalloid, have been classified as high-priority pollutants. Increasing Sb released into the water environment by natural processes and anthropogenic activities, which exposure threatens to human health and ecosystems. Therefore, it is of unquestionable importance to remove Sb from polluted water. Keeping in view the extreme importance of this issue, we summarize the source, chemistry, speciation, distribution, toxicity, and polluted situation of Sb about aqueous solution. Then, we provide the recent and common technology to remove Sb, which are based on adsorption, coagulation/flocculation, electrochemical technology, membrane technology, ion exchange, etc. In this review, we focus in detail on the adsorption method, researchers at present have been investigating to discover more advanced, cost-effective, eco-friendly, reusable adsorbents. However, to date the Sb-containing wastewater treatment technologies are not sufficiently developed and most of research have been tested only in controlled lab conditions. Few reports are available that include field studies and applications. We critically analyzed the salient features and removal mechanisms, evaluating benefits and limitations of these technologies, hoping to provide more references for further research. Finally, we considered the Fe- or Mn-based technologies was the most promising technique to remove Sb for field application.     

Exfoliated Mg–Al–Fe layered double hydroxides/polyether sulfone mixed matrix membranes for adsorption of phosphate and fluoride from aqueous solutions

Mg–Al–Fe layered double hydroxides(LDHs) were exfoliated and incorporated in polyether sulfone membranes for the removal of phosphate and fluoride for the first time. The exfoliation methods, coagulation bath, LDH amount, interfering ions, adsorption isotherm,desorption and reuse of the membranes were investigated. It was found that LDHs could be quickly exfoliated in formamide/N,N-dimethylformamide(DMF) solvent mixtures with sodium carboxymethyl cellulose as a stabilizer. The membranes displayed much higher adsorption capacity for phosphate(5.61 mg/g) and faster adsorption rate than the unexfoliated materials. With increased DMF content in the coagulation bath, the static and dynamic adsorption capacity rose. Interference from Cl-and SO_4~(2-)(50 mg/L) on adsorption of phosphates was not apparent. The membranes displayed excellent reusability in dynamic adsorption/desorption. The membranes also showed high adsorption capacity for fluorides(1.61 mg/g).     

膜技术在工业废水处理中的应用

膜技术是一种高效率、低能耗和易操作的液体分离技术，在废水处理中得到越来越广泛的应用。在介绍膜技术分类和分离机理的基础上，对膜技术在造纸废水、重金属废水、含油废水、印染废水、食品废水等工业废水处理中的应用进行了综述，最后对膜技术在工业废水处理的应用前景作了展望。     

Membrane fouling in ultrafiltration of natural water after pretreatment to different extents

The combined fouling during ultrafiltration(UF) of surface water pretreated to different extents was investigated to disclose the roles of polysaccharides, proteins, and inorganic particles in UF membrane fouling. Both reversible and irreversible fouling decreased with enhanced pretreatment(biologically active carbon(BAC) treatment and sand filtration). The sand filter effluent fouled the membrane very slowly. The UF membrane removed turbidity to less than 0.1 nephelometric turbidity unit(NTU), reduced polysaccharides by 25.4%–29.9%, but rejected few proteins. Both polysaccharides and inorganic particles were detected on the fouled membranes, but inorganic particles could be effectively removed by backwashing. The increase of turbidity in the sand filter effluent to 3.05 NTU did not significantly increase the fouling rate, but an increase in the turbidity in the BAC effluent to6.11 NTU increased the fouling rate by more than 100%. The results demonstrated that the polysaccharide, not the protein, constituents of biopolymers were responsible for membrane fouling. Membrane fouling was closely associated with a small fraction of polysaccharides in the feed water. Inorganic particles exacerbated membrane fouling only when the concentration of fouling–inducing polysaccharides in the feed water was relatively high. The combined fouling was largely reversible, and polysaccharides were the predominant substances responsible for irreversible fouling.