贵州关岭晚三叠世早期海生爬行动物Neosinasaurusnom.nov.

笔者在研究关岭晚三叠世早期海生爬行动物(见本刊上期1～23页)时曾命名中国龙属Sinasaurus Zhou (2000).现发现,"Sinasaurus"这个属名早在1940年就已被杨钟健教授研究描述肉食恐龙类Sinosaurus Young (1940)(见Young Z.J., Bull. Geol. Soc. China, 1940,XX (3～4):235～240)时所占用,Sinasaurus是晚出名,应废弃不用,现给与新名Neosinasaurus Zhou, nom. nov. 而替代Sinasaurus Zhou (2000).因Sinasaurus Zhou (2000) 为中国龙科的模式属,故将Sinasauridae Zhou (2000) 更名为新中国龙科(新名)Neosinasauridae Zhou nom.nov..现将Neosinasaurus和Xinpusaurus的分类位置列述如下     

前屯煤矿矿井水处理作饮用水的技术实践

本文根据前屯煤矿矿井水排放规律和原水水质特征，采用ＫＪＳ型一体化净水器，锰砂除铁滤器及消毒等处理工艺，处理后水质完全达到国家饮用水标准，工程投资和运行费用均较合理。     

Selective extraction of trace mercury and cadmium from drinking water sources.

In this paper, a new alternative method, i.e., selective extraction by weakly basic anion exchange resin, has been developed for the removal of trace cadmium and mercury ions from drinking water sources. The mechanism of heavy metal removal is based on selective extraction as the results of LEWIS-base-acid interactions. Transfer of trace mercury species from liquid to resin phase coincides well with the performance of film diffusion. The results demonstrated that the presence of chlorine has a negligible influence on the removal of mercury. However, humic acids can strongly bind mercury by the formation of complex compounds and therefore become the obstacle in the diffusion progress. At neutral or base pH, the resin material exhibits the favorable uptake of heavy metals. In filter experiments, the studied resin material offers favorable properties in the selective extraction of trace mercury and cadmium.     

论我国环境侵权救济法律制度的完善

环境侵权是随着工业化和城市化的发展而出现的新型侵权行为之一。随着中国经济的迅速发展，由环境污染和生态破坏造成的环境污染侵权现象及其救济已成为中国的一大社会问题。中国目前尚缺乏对环境侵权救济法律制度的全面深入研究，有关立法也不完善，而西方发达国家有关环境侵权救济法的理论和实践已经较为成熟。拟借鉴西方国家的环境侵权救济法律制度，并立足中国国情，提出了完善中国环境侵权救济法律制度的若干建议。     

手性污染物环境行为的对映体差异性

环境中手性污染物对映体选择性行为的研究历史不长 ,但由于手性化合物对映体生物活性的差异性 ,手性污染物在环境中的对映体选择性行为已愈来愈引起人们的关注。本文对近 10多年来手性污染物的环境行为研究进行全面评述     

Experimental study on the removal of PAHs using in-duct activated carbon injection

This paper presents the incineration tests of municipal solid waste (MSW) in a fluidized bed and the adsorption of activated carbon (AC) on polycyclic aromatic hydrocarbons (PAHs). An extraction and high performance liquid chromatography (HPLC) technique was used to analyze the concentrations of the 16 US EPA specified PAHs contained in raw MSW, flue gas, fly ash, and bottom ash. The aim of this work was to decide the influence of AC on the distribution of PAHs during the incineration of MSW. Experimental researches show that there were a few PAHs in MSW and bottom ash. With the increase of AC feeding rate, the concentrations of three- to six-ring PAHs in fly ash increased, and the concentration of two-ring PAH decreased. The total-PAHs in flue gas were dominated by three-, and four-ring PAHs, but a few two-, five-ring PAHs and no six-ring PAHs were found. PAHs could be removed effectively from flue gas by using in-duct AC injection and the removal efficiencies of PAHs were about 76-91%. In addition, the total toxic equivalent (TEQ) concentrations of PAH in raw MSW, bottom ash, fly ash, and flue gas were 1.24 mg TEQ kg-1, 0.25 mg TEQ kg-1, 6.89-9.67 mg TEQ kg-1, and 0.36-1.50 microg TEQ Nm-3, respectively.     

污染土壤修复效果评定方法的研究

在实施污染土壤修复的环境工程后,需要通过灵敏和有效的评定方法对污染土壤修复的效果进行评定.然而,单纯依靠化学方法进行污染土壤修复效果的评定,不能揭示土壤的整体质量特征,因此需要生态毒理方法作为相互补充的手段.本文概述了植物毒性评定法、陆生无脊椎动物评定法和土壤微生物评定法及其在污染土壤修复效果评定中的应用,并对污染土壤修复效果评定方法的发展前景进行展望.     

UV/Fenton法处理间-甲酚废水

利用UV/Fenton工艺对模拟间-甲苯酚废水进行了处理,研究了H2O2加入量、FeSO4加入量、pH、原水初始COD值、环境温度、反应时间等因素对COD去除率的影响.实验表明:间-甲苯酚浓度为100mg/L、初始COD值251 mg/L的废水,在30℃下,pH为4.Q,[H2O2]/[Fe2 ]=15(质量浓度比),紫外灯照射3 h后,COD去除率达86.3%,若再经Ca(OH)2絮凝沉降,则COD去除率提高到92.6%.同时,对Fenton及UV/Fenton的处理效果进行了比较,实验表明:UV/Fenton的处理效果明显优于Fenton法.     

活性炭纤维吸附废水中对硝基苯酚及其脱附研究

采用新型高效吸附剂——活性炭纤维吸附废水中对硝基苯酚，对其吸附和脱附影响因素进行了较详细的研究，确定了最佳工艺参数，并对动态吸附一脱附进行了稳定性实验。在最佳的吸附条件下，装填4g活性炭纤维可处理含对硝基苯酚1000mg/L的废水1400mL，出水对硝基苯酚浓度〈2mg／L，达到国家综合污水一级排放标准，活性炭纤维有效吸附量可达349．87mg／g。在最佳脱附条件下，脱附率〉99％，并可从高浓度脱附液中回收对硝基苯酚。稳定性实验表明，吸附-脱附性能稳定，采用活性炭纤维吸附处理对硝基苯酚废水是一种行之有效的处理方法。     

啤酒生产废水处理设计及运行研究

分析了年产15万t啤酒的生产废水情况,介绍了采用IC厌氧反应器-一体化氧化沟处理该生产废水(7 200 m3/d)的工艺路线和主要设计参数,讨论了废水处理系统的运行情况.其中IC厌氧反应器的HRT为8 h,运行温度为35～37 ℃;一体化氧化沟包括氧化沟段和沉淀池段,总尺寸为40 m×24 m×6 m.IC厌氧反应器COD容积负荷在7.78 kg/(m3·d)时,COD去除率为84%左右.整套废水处理系统的COD总去除率为98%左右,出水COD小于80 mg/L.厌氧所产生的沼气可用于废水的升温.