旋流器在船舶舱底含油污水分离中的应用

分析了船舶舱底含油污水的特性，讨论了船舶油水分离器的现状及使用中存在的问题，提出了使用旋流器对船舶舱底含油污水进行预处理，以改善进入船舶油水分离器的水质及减轻管理人员负担。     

用主成分分析法研究评价地下水质量——以邯郸市为例

运用主成分分析法(PCA)对邯郸市地下水主要污染指标年均值进行了探索性评价研究。分析结果表明,前5个主成分综合携带了全部信息的91.374%。通过对这5个新的综合指标进行分析,确定了地下水的主要污染物,同时根据其综合得分对地下水进行分级,分析了其变化趋势,为地下水资源的有效利用和保护提供了科学依据。     

Utilization of Bagasse Energy in Thailand

Bagasse, a biomass fuel, is the waste generated by the sugar-making process from sugar cane. Sugar making is one of the most important agricultural-produce processing industries for developing countries in Southeast Asia, Latin America and Africa. As sugar producing plants need electric power and process steam, co-generation using bagasse as an alternate fuel for petroleum has been in use for some time. Thailand recently became one of the largest sugar exporters by enlarging plant capacities and improving equipment, thus reducing its production cost. In addition, the Thai government promotes power generation using bagasse as a means to combat global warming by raising the purchase price of the surplus power. The industry is in the process of further raising the plant capacity, and improving the power-generating efficiency. This will enable a plant to generate more electric power than its in-plant need so that the surplus power can be sold to the commercial grid. It also plans to become a local power supplier during off-season of sugar making by adding a condensing turbine generator. A typical Thai sugar plant of the latest design generates steam of 4Mpa at the bagasse boiler outlet with the temperature of 400°C at 84% boiler efficiency. With the bagasse LHV of 7,540 kJ/kg and that of fuel oil 41, 840 kJ/kg, and taking 90%as oil-burning boiler efficiency, 5.95 kg of bagasse would replace 1 kg of oil. The Kyoto Mechanism defines CO₂ generation by fuel oil as 2.65 kg per liter. Using 0.85for the specific gravity of fuel oil, the amount of CO₂ generation will be 3.12 kg-CO₂/kg. Therefore, CO₂reduction per ton of bagasse in terms of fuel oil will be: 3.12/5.95 =0.524 kg-CO₂/kg-bagasse. As 1 kg of bagasse generates 2 kg of steam, the CO₂reduction of a 100t/h steam boiler will be112,660 ton/year for an annual operation of4,300 hours, as follows. 0.524 × 100/2 = 26.2 t-CO₂/h, 26.2 × 4,300 =112,660 t-CO₂/year. This revised version was published online in August 2006 with corrections to the Cover Date.     

浅谈“三道防线”对防止污染水域的作用

在简要介绍了上海港散装液体危险装货物储运作业发展的基础上，分析了码头装卸作用中存在的防污染问题，提出了“三道防线”是防止污染的有效措施。     

某糠醛厂排放废水及周围地下水的GC/MS测定

某地地下水显淡黄色有异味，为查明被污染原因，我们利用ＧＤＸ－１０２树脂富集，对该处唯一的一家工厂——某糠醛厂排放的废水及其周围地下水同时进行了ＧＣ／ＭＳ测定．以上两种水体中均有呋喃类化合物（包括糠醛）及酚类化合物检出，而远离工厂的上游地下水未发现以上两类化合物，这一结果表明，该地下水区被工厂排放的废水所污染     

天然水体及生活饮用水中铝的含量及形态分布

采用ＰＣＶ络合比色法和Ｆｅｒｒｏｎ逐时络合比色法，选取３种典型环境中的水体为研究对象；江西德兴铜矿地区的乐安江，白洋淀地区以及从源水，自来水到铝锅煮沸水序列水样，着重分析其中铝的含量及其形态分布，并讨论了铝的含量及其形态的变化对３种典型环境的影响。     

水体中挥发酚自净模式研究

采用均匀设计法设计实验，当实验条件曝气强度（ml/min)、酚的起始浓度（mg/l)、加入底泥量（g)、加入10%HgCl2量（ml)、处理温度（℃）、处理时间（小时）分别用X1、X2、X3、X4、X5、X6表示时，得到它们与含酚污水中总酚去除率Y和挥发除去酚浓度C的关系分别为：Y=-100.67 21.835Lnx1 17.920Lnx2 1.595√x3-0.124x4 1.131x5-1.086e^x6;C=-3.308 0.614Lnx1 0.307Lnx2 0.179√x3 5.100*10^-2x4 2.369*10^-2x5-0.692Lnx6。并讨论了酚在水体中自净的规律。     

MF微生物絮凝剂的制备与应用

介绍了 MF微生物絮凝剂的制备过程及其在畜产废水、建筑材料加工废水等方面的应用 ,同时对微生物絮凝剂的开发提出建议     

膜法水处理技术及研究进展

综述了反渗透、微滤、超滤、纳滤、渗透蒸发、液膜等几种常见膜技术的应用现状及进展情况 ,主要对反渗透膜的原理、流程、存在的问题及开发和利用情况进行了介绍。简单概括了近年发展起来的双极膜等新膜分离技术的开发研究。展望了膜分离技术的前景     

水解酸化—厌氧工艺处理高浓度抗生素废水研究

研究了水解酸化与厌氧消化组合工艺处理高浓度抗生素废水,结果表明,水解酸化反应器最大CODcr容积负荷达到 16.84kg/m3·d,复合厌氧反应器CODcr容积负荷达到8.57kg/m3·d;系统进水SO42-浓度为1325mg/L,CODcr/SO42-值最低达到 3;CODCr与SO42-总去除率分别为75.5％和95.2％,对各种抑制物质和冲击负荷表现出很好的适应性。