循环冷却水复配阻垢缓蚀剂配方的优化

阐述了循环冷却水对金属腐蚀的机理、阻垢缓蚀剂作用的原理,提出了复配缓蚀阻垢剂配方优化的原则及评价标准。并对攀钢煤化公司循环冷却水进行了复配缓蚀阻垢剂配方优化试验,通过配方优化试验,筛选出了DS—605型(浓度为100mg/L)的高效低磷有机膦阻垢缓蚀剂。该配方技术先进,其阻垢缓蚀效果优于GB/50050—95规定的指标要求,冷却水磷含量由原先的12mg/L降至6mg/L,年处理费用降低了27%,具有显著的经济效益和环保效益,目前正准备投入实际使用。     

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.     

生物滤池和常规工艺对某地表水中不同分子量有机物的去除

采用生物滤池和常规处理对受污染的某地表水进行试验研究 ,用膜过滤法对其出水进行了分子量分析 ,考察了 2个处理单元对不同分子量区间有机物的去除效果。结果表明 :原水中分子量小于 1 0 0 0的有机物占总 DOC的 78.2 9% ;生物滤池对分子量小于50 0、50 0～ 1 0 0 0和 >60 0 0 0的有机物去除率分别为 54.9%、36.1 %和 2 0 .7% ;常规处理对以上分子量区间有机物的去除率分别为1 5.3%、- 2 0 %和 48.75%。     

稠联污水生化处理技术研究

河南油田在可行性研究的基础上，开展了生化技术处理稠油联合站污水的现场实验研究。结果表明，采用生化技术处理后的外排水主要监测指标COD为70～100mg／L，油含量为4～6mg／L，悬浮物35～45mg／L，其它指标达到了有关排放标准。     

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。     

活性污泥数学模型中进水易降解有机物的测定

ASM系列模型 (ASMs)自推出以来在欧美得到广泛应用。要想利用ASMs对特定污水处理过程进行准确的模拟 ,首先必须得到该过程污水的水质特性参数。介绍了连续式OUR计量法、序批式OUR计量法和絮凝过滤物理化学法等 3种测定ASMs中进水易降解有机物的方法 ,通过分析比较指出了各自的优缺点及适用情况。     

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     

生物作用强化城市污水一级处理工艺研究

提出生物作用强化城市污水一级处理工艺 ,探讨利用生物絮凝吸附作用独立承担城市污水处理任务的可行性、影响因素及运行参数。试验证明 ,处理城市污水 ,当HRT为 1 1h ,DO为 1 0mg L ,CODCr污泥负荷为 3 4～ 4 0kg kg·d时 ,CODCr、BOD5和SS去除率分别为 6 8%～ 78%、6 5 %～ 72 %和 75 %～ 85 %。     

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.