冲击水浴除尘器密闭式水位控制箱的研制

通过对的冲击水浴除尘器存在运行工况不稳定等问题的分析，介绍了一种能提高除尘器净化效率，稳定设备运行阻力的新型水位控制箱。     

种子发芽势在环境污染监测中作为生物指标的尝试

本文用测定种子发芽势的方法，对Ｃｄ２＋、Ｈｇ２＋Ａｓ３－的生物毒害效应进行了试验，结果表明，种子发芽指数能很好地反映不同浓度Ｃｄ２＋、Ｈｇ２＋、Ａｓ３－的生物毒害作用．种子发芽势试验也可用于多成分污染物的生物毒性判别，通过相关分析或复回归分析可以大致判别出多成分污染物中何种成分生物毒性大．     

氯氟烃及其替代物

近年来,臭氧衰竭比原先预料的更严重,对人类健康和环境构成了严重威胁。“蒙特利尔议定书”和“大气清洁法案”要求2000年要完全清除致臭氧衰竭物质——氯氟烃(CFCs)的生产和使用。目前,世界各地积极开发CFCs的替代物,以加速转换。虽然已开发的氧氯氟烃(HCFCs)、氢氟烃(HFCs)等替代物与CFCs相比还有一定缺点,但最终一定会实现替代转换。     

利用pH值梯度研究建筑砂浆的酸蚀程度

在两种不同ｐＨ值模拟酸雨和３种浸泡时间条件下，据ｐＨ值梯度测定了各类保护剂处理建筑砂浆试件的酸化层厚度，从而判定保护剂的保护效果，了解酸蚀程度。并分析了影响酸化层厚度的因素。     

UASB装置处理溶剂生产废醪液

本文介绍了采用ＵＡＳＢ装置处理发酵法溶剂生产的废醪液工艺过程．总结了在生产实践中遇到的问题，及解决问题的方法和工艺控制点的选择．说明用ＵＡＳＢ装置处理废醪液是一种很好的方法．     

电子废弃物的特点

电子废弃物资源化研究是一项新型而紧迫的课题，它具有数量多、危害大、潜在价值高、回收利用困难的特点，必须对电子废弃物予以高度关注。     

用萃取法处理含苯胺废水的研究

本文介绍了以甲苯做萃取剂萃取硫化橡胶促进剂生产废水中苯胺类物质的方法,确定了萃取级数、萃取剂配比 和萃取时间等工艺参数。经过萃取,废水中的苯胺类物质与化学需氧量的去除率分别达95％和88％以上,萃取后的废水 可以进行生化处理。     

唐钢一炼钢厂VD精炼炉直接冷却水系统设计

介绍了VD精炼炉直接冷却水处理常用的工艺流程及设计中应重点考虑的问题 ,如水处理单元的选择 ,供水泵与提升泵的匹配问题等     

2-Chlorophenol oxidation kinetic by photo-assisted Fenton process

Experimental data are presented to test and validate a kinetic model for the oxidation of 2-chlorophenol wastewater by photo-assisted Fenton process. The data showed that this process had produced good effects under acidic conductions. Up to 90% 2-chlorophenol was removed after 90-minute reaction time with H2O2 of 25% CODCr. in, while in UV/H2O2 system ordy 16.8% 2-chlorophenol was removed after one hour treatment. The optimal pH in this reaction occurred between pH 3.0 and pH 4.0. The reaction kinetics for photo-assisted Fenton process experimented in this research was investigated. Kinetic models were proposed for the treatment of 2-chlorophenol wastewater. The reaction was found to follow the 2nd order. The equations of reaction kinetics are as follows:-d[RH]/dt=KRH[RH][H2O2]0exp(-KH2o2t);-d[CODCr]/dt=KCODCr[CODCr][H2O2]0exp(-K′t).The prediction of the models was found to be in a good agreement with experimental results, thus confimfing the proposed reaction mechanism.     

Catalysts for decomposing ozone tail gas

The preparation of immobilizing-catalysts for decomposing ozone by using dipping method was studied. XRD, XPS and TEM were used to characterize the catalysts. The three kinds of catalysts were selected preferentially, and their catalytic activities were investigated. The results showed that the catalyst with activated carbon dipping acetate( active components are Mn:Cu = 3:2, active component proportion in catalyst is 15%, calcination temperature is 200℃ ) has the best catalytic activity for ozone decomposing. One gram of catalyst can decompose 17.6g ozone at initial ozone concentration of 2.5g/m^3 and the residence time in reactor of 0.1s. The experimental results also indicated that humidity of reaction system had negative effect on catalytic activity.