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381.
危险废物分类、识别、监控一体化管理技术研究概述 总被引:1,自引:0,他引:1
研究运用环境统计信息系统(ESIS),建立黑龙江省典型危险废物的数据库系统,使其具备系统、完善的查询与追踪功能;提出危险废物易燃性、腐蚀性、反应性和毒性方面定量化的定义,建立基于危险废物成分分析基础上的分类体系,使危险废物的处理与处置具有良好的可操作性;开发危险废物在线识别技术,促进对危险废物进行监管及预警的时效性和有效性;运用GPS、GSM、GPRS、GIS、计算机网络通信和数据处理等监控技术,实施对危险废物运输车辆的远程在线监控;提出危险废物收集、贮存、分离、运输、处理、处置、回收利用过程中的管理法律、法规,促进危险废物全过程管理的有效实现. 相似文献
382.
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 总被引:1,自引:0,他引:1
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%。 相似文献
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385.
Heavy metals in surface sediments from Minjiang Esturary—Mazu and Xiamen—Jinmen sea areas 总被引:4,自引:0,他引:4
The concentrations of Cu,Pb, Zn and Cd in surface sediments from Minjang Estuary-Mazu and Ziamen-Jinmen sea areas of China were investigated during 1995-1996.The concentration ranges of Cu,Pb ,Zn and Cd in the Minjiang Estuary-Mazu sea area were 16.4-37.2,33.4-69.6,92.1-128,0.087-0.036mg/kg(dry wt.),respectively; those for Xiamen-Jinmen sea area were 11.0-24.5,36.0-80.3,77.5-161,0.135-0.285mg/kg(dry wt.), respectively.The concentration and distributions of Cu,Pb,Zn and Cd in surface sediments of Minjiang Estuary-Mazu and Xiamen-Jinmen sea areas were analyzed and evaluated.The results showed that the values of Zn and Pb exceeded those of sediment quality criteria.The average concentration of Cu in Minjiang Estuary-Mazu sea area was higher than that in Xiamen-Jinmen sea area.The obviously higher concentrations of Cu,Pb, Zn and Cd were found at outlets of Minjiang and Jiulong River.From the estuaries to open sea, the concentrations of Cu, Pb,Zn and Cd had a decreasing trend, and then elevated in the sea areas near Mazu and Jinmen, suggesting that Cu,Pb,Zn and Cd in Minjiang Estuary-Mazu and Xiamen-Jinmen sea areas may come from both the mainland and Taiwan of China. 相似文献
386.
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. 相似文献
387.
IntroductionChlorinatedorganiccompoundshavebeenusedonalargescaleinthechemical,petrochemical,andelectronicindustries.Inrecentyears ,worldwideattentionhasbeengiventotheenvironmentalandhealthimpactofthemasaclassofcontaminants .Severalareknowntocauseozonedepletion ,whileothersproduceadverseeffectsonthehumancentralnervoussystemandhavebeenlinkedtodiseasessuchascancer.Almostallofthechlorinatedaromaticcompoundsaretoxicandthermallystable .Oncereleasedintoenvironment,theywillaccumulateinthesurroundings… 相似文献
388.
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. 相似文献
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