小康居住区的水环境与水质净化工程

分析了小康居住区水环境的含义，组成，并对居住区水质净化工程中3个热点问题（优质饮水，污水处理和中水回用等）进行了较深入的分析，建议小康居住区优质饮水供应以小区纯水站净化，管理输送至用户方式为主；不居住区的污水处理应分3种情况区别对待，在居住区污水处理达到排放标准的基础上，进一步处理回用，是经济合理的。     

洛阳分公司恶臭污染调查及防治

分析了洛阳分公司恶臭污染源，提出了解决恶臭污染的常用方法及对洛阳分公司恶臭污染源的控制及治理途径。     

色基生产废水的三级处理工艺试验

在染料中间体红色基Ｂ，紫酱色基ＧＰ的生产过程中，全产生降解处理的废水，采用中和隔油－生物接触氧化－电解脱色工艺处理可达标准排放。试验结果表明，硝化废酸液和水解母液的混合废水经过中和隔油处理后，ＣＯＤｃｒ的去除率可达到５６％以上，而ＢＯＤ５／ＣＤＯｃｒ的比值可在从０．２２提高到０．５以上；再经生物接触氧化处理后，ＣＯＤｃｒ的去除率在８８％以上，ＢＯＤ５的去除率在９２％以上；最后，电解处理能使ＣＯＤｃ     

JHX新型浮选机在处理含油污水中的应用

介绍JHX新型高效射流浮选机在处理含油污水中的应用，考察各种工艺条件下JHX浮选机的工作情况，JHX浮选机由于其独特的发泡原理和结构设计，对含油污水有很高的除油效率。     

炼油厂污水处理负荷的削减措施

总结和分析了某厂削减污水处理负荷的主要措施及效益，预测该厂在达到16000kt/a以上加工规模时的污水处理负荷。     

电泳油漆废水凝聚处理研究

以高浓度电泳漆废水用酸性凝聚和碱性凝聚进行处理研究，应用结果表明，在控制ＰＨ＝２．５～３条件下进行酸性凝聚，ＣＯＤ去除率可达９１％～９３％酸性凝聚后出水，与低浓度废水混合，再用ＰＦＳ为凝聚剂，控制ＰＨ＝７～９，进行凝聚气浮处理，可使排放水质中ＣＯＤ，ＰＨ，ＳＳ和色度稳定达标。     

氧化塘合理的设计与操作

氧化塘不但可以低费用的降解废水，而且可以提供有用的生物量，其关键是进行合理的设计、操作和去除污泥．本文综合国外的文献资料，提出合理的设计和操作方案，并且引用国外试验者开发的预测模型；同时提出操作过程加入适当的ＣａＣｌ２化学添加剂可以促进藻类生物量的絮凝，以保证出水的质量和提供可利用的生物量．     

聚合硫酸铁对几种有机废水的处理效果初探

比较了聚合硫酸铁对五种有机废水的处理效果，并探讨了聚铁对不同分子量有机物模拟废水的ＣＯＤｃｒ去除率与废水有机物分子量之间的关系．结果表明：聚铁对有机废水ＣＯＤｃｒ去除率随废水主成分的分子量上升而呈上升趋势，废水有机成分分子量在３００～４００以上时，聚铁处理有机废水效果较好．     

浅析江苏油田井下作业清洁生产工艺技术

以江苏油田井下作业清洁生产工艺为例，分析了井下作业施工造成对环境污染的因素，介绍了江苏油田在井下作业前期、中期、后期清洁生产的措施及其相关配套新工艺、新技术的应用和取得的效果。     

Graphical strategies for design of evaporation crystallization networks for environmental wastewater applications

This paper introduces graphical strategies for the design of an evaporation/crystallization network for ternary wastewater environmental applications. Sources, sinks and other streams are located on a ternary composition diagram. While a source is any wastewater stream that has the potential to be recycled, a sink is any unit in the process that can accept sources. The proposed methodology is extremely simple to understand and implement, as it only requires basic solid-liquid phase equilibria data and uses lever arm principles to generate alternative process designs. Geometric constructions are carried out on the ternary composition diagram and the respective lever arms are used to determine intermediate flow rates in the evaporation/crystallization network. The relative locations and flow rates of the sources and sinks under consideration, as well as the unique shape of the solid-liquid equilibrium, drive the design of the separation (via evaporation/crystallization) network. Some generic structures are proposed for a typical evaporation and crystallization network. Once the general problem statement has been defined, special cases consisting of a single source-single sink, single source-two sinks and two sources-single sink are described. These special cases are representative of commonly occurring industrial wastewater design problems. Several graphical insights are listed that allow one to represent evaporation and crystallization operations on a ternary triangular composition diagram and avoid mathematical complexity. The possibility of bypassing a part of the initial feed streams is also considered. Certain feasible composition regions are identified on the ternary composition diagram for cases dealing with multiple sources and sinks. The methodology is useful in pre-screening and eliminating certain sources/sinks and is readily applicable to cases with lower number of sources and sinks. A case study involving the ammonium nitrate manufacturing process is included to demonstrate the broad applicability and value of the proposed approach.