水解酸化＋两级生物接触氧化处理高盐度水产品加工废水

介绍了“水解酸化＋两级生物接触氧化”处理水产品加工废水的运行效果和工程实例，结果表明：对C1^-浓度平均6000mg／L的高盐度水产品加工废水，系统对COD、SS、氨氮的去除率分别超过了88％、90％、85％，出水COD、SS、氨氮分别低于100mg／L、70mg／L、15mg／L，出水完全可以达到《污水综合排放标准》（GB8978—1996）一级排放标准。     

玉溪市环境空气质量及污染物分布状况研究

分析了2002年玉溪市各县区县城环境空气质量状况和污染特征 提出应采取措施,减轻SO2,对城市大气的污染。     

京津地区能源、大气污染物扩散对区域元素循环的作用

对京津区域１９８０－１９９２年间能源利用状况进行分析，并通过模式计算该区域大气污染物的扩散规律，结果表明，大气污染物随能源利用增加而增加，其增加速率ＮＯｘ大于ＯＳ２，经预测，至２００４年京津地区ＳＯ２排放量增咖１１．４０％，ＮＯｘ增加５６．８０％，由于气象和地形条件所致，该区域内不利于大气污染物远距离输送，这使箱型区域内物料平衡计算可以简化。     

Effects of atmospheric gases on terrestrial plants and critical levels of air pollution

An integrated approach was developed to determine the critical levels of air pollution for ecological standard setting based on the unified index of biological response, by taking into account the effects of all pollution components simultaneously. An empirical model of plant productivity was taken as the dose response model for gaseous pollutant effect on the productivity of trees and the annual productivity of plants was used as the above mentioned index. The CO2 increase in the lower atmosphere was considered to potentially increase plant productivity and NO2 was estimated as neutral while being dangerous for plants as a chemical precursor of ozone or as a source of acidification. The maximum permissible chronic O3 and SO2 levels for trees were estimated and it was found that O3 is much more phytotoxic, as compared to SO2 , with a rather narrow range of permissible levels (27-33 ppb) which complicates its monitoring and control.     

关于环境生物技术在水污染治理中的研究与应用

分析了国内外关于微生物遗传学、酶学在环境生物技术领域中的研究进展以及环境生物技术在污水治理学的开发与应用及其发展趋势，为选择实用的污水处理技术提供了参考依据。     

运用生物循环理论建立多元生物污水处理新工艺

以活性污泥法为主流工艺的现代污水处理技术,存在着工程投资大，运行费用高，管理复杂等缺点，按照生物循环基本理论要示是不完善的。多元生物污水处理是按照食物链代谢规律,运有生物循环理论，设计成微生物－植物－水生动物3个处理单元。污水中的有机物作为微生物人良料在第1单元被套氧微生物消化降解成CO2，H2O，NH^ 4,CH^-4等，除CH4作为生物能源可回收利用外，其它物质是植物的营养物质，在第2单元藻类等多种植物吸收，通过光合作用合成植物细胞，并释放氧气，在第1单元和第2单元增殖的细胞和藻类成为水生动物的食料，在第3单元被浮游动物和鱼类捕食，转化成动物蛋白，污水中的有机物在3个单元组成的生态净化系统中，被多样生物逐级利用，最终转化成植物细胞和动物蛋白，使污水得到净化，达到三级处理水平，不产生二次污 ，是一种安全的，对环境友好的污水处理新技术，在国外被誉为21世纪的新科技。该污水净化系统，按照生物循环基本理论进行工艺设计，通过生态平衡自我调控，具有工艺流程简单，投资省，运行费用低，管理简便等优点，适合我国国情，有广阔的应用前景，尤其适有于小城镇污水处理。     

Treatment of a dyeing wastewater from a woolen mill using an A/O membrane bio-reactor

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浅谈我国室内环境污染的来源、危害及防治现状

分析了我国室内环境主要污染物的来源，以及这些污染物给人们带来的危害；并阐述了目前我国室内环境保护方面的现状及对策。     

染化废水厌氧生物处理技术的研究

鉴于厌氧微生物对偶氮染料的还原裂解作用，开发了以易降解工业有机废水作为外加碳源的染化废水厌氧生物处理的新技术．试验结果表明：在进水ＣＯＤ３１００—３５００ｍｇ／Ｌ，ＣＯＤ总／ＣＯＤ染化比值４０，ＨＲＴ３．０ｄ下，ＣＯＤ去除率＞８０％，最低染化ＣＯＤ去除率＞４５％，色度去除率＞８５％；实验证实，在厌氧处理过程中，染料组分的结构已发生了明显的变化；反应器内的污泥大多呈颗粒状；污泥活性和工艺性能可控制工艺运行参数得以维持．     

Test of membrane bioreactor for waste water treatment in a petrochemical complex

Membrane bioreactor (MBR) used in water and waste water treatment is a developing technique for water pollution control and water reuse. This paper describes a membrane-bioreactor for treatment of waste water in a petrochemical complex. The experimental MBR was a lab scale one composed of an activated sludge bioreactor unit and an ultrafiltration membrane unit. The relationship of COD removal with MLSS and HRT in this MBR was studied. The effects of crossflow velocity, backwash interval and volume of flush liquid on the flux were discussed. The results showed that average removal of COD, oil, SS and turbidity in petrochemical waste water by the MBR was 91%, 86%, 92% and 99% respectively. The average removal of NH₃-N and total phosphorous was 85% and 82%. A coefficient of COD removal, k, was 0.017-0.080 L/(mg.d). The membrane flux maintained higher than 60 L/hm2 bar for 34 days without chemical cleaning when the velocity of crossflow was 3.5-3.9 m/s and the backwash interval was 30 minutes and backwash duration at 20 seconds. The results indicated that it is feasible for MBR technology to be used in petrochemical waste water treatment. The treated water could be considered as a source used to make up water for industrial cooling system or to be reused for other purposes.