植物多酚物质原位钝化污染土壤重金属的研究Ⅱ.对土壤Cu环境行为和生物活性的影响动态

通过室内好气培养和生物盆栽试验研究了缩合类植物多酚L和Y以及 8 羟基喹啉在污染红壤和潮土中的降解动态及其对土壤Cu环境行为的影响 .结果表明植物多酚在两周内降解相对较快 ,而 8 羟基喹啉则难以降解 .与空白相比 ,Cu污染土壤中施用植物多酚后土壤水溶性Cu显著下降 ,钝化Cu的效果次序为 :8 羟基喹啉 >多酚Y >多酚L .随着植物多酚的降解 ,土壤Cu被释出 ,其水溶性Cu浓度与残留在土壤中多酚浓度 (以DOC浓度表示 )呈负相关关系 ,尤其在潮土上更为明显 ,而pH与水溶性Cu没有相关性 .试验还发现 ,钝化剂施用后 ,小麦体内的Cu含量降低 ,因此 ,植物多酚是钝化重金属污染土壤的良好选择     

Effect of airborne SO_2 on performance of the turnip moth,Agrotis segetum Schiff

SO2 Pollution; rape plant (Brassica chinensis); turnip moth (Agrotis segetum); growth and developmental parameters.     

厌氧-混凝工艺处理造纸厂终端废水试验研究

本文报告了用厌氧 -混凝工艺处理造纸厂终端废水的实验情况 ,在最佳实验条件下 ,废水从CODcr80 6 . 7m g/ L、BOD52 10 . 5 m g/ L、SS2 15 . 7m g/ L、OD4 650 . 35 0降至 CODcr6 1. 5 m g/ L、BOD52 7. 4m g/ L、SS17.3mg/ L、OD4 650 .0 11。实验结果表明对造纸厂终端废水的治理 ,本工艺是很有实用价值的一种方法     

Effects of atmospheric mercury pollution on terrestrial ecosystem in Chongqing, China

1　ＩｎｔｒｏｄｕｃｔｉｏｎＭｅｒｃｕｒｙ(Ｈｇ)ａｓａｇｌｏｂａｌｐｏｌｌｕｔａｎｔｈａｓｃａｕｓｅｄｃｏｎｃｅｒｎｗｏｒｌｄｗｉｄｅｓｉｎｃｅｔｈｅｅｎｄｏｆ 1980ｓ.Ｉｔｉｓｅｍｉｔｔｅｄｔｏｔｈｅａｔｍｏｓｐｈｅｒｅｆｒｏｍｂｏｔｈａｎｔｈｒｏｐｏｇｅｎｉｃａｎｄｎａｔｕｒａｌｓｏｕｒｃｅｓ.Ｉｍｐｏｒｔａｎｔｓｏｕｒｃｅｏｆｔｈｅｆｏｒｍｅｒｉｓｔｈｅｄｉｓｃｈａｒｇｅｆｒｏｍ ｐｒｏｄｕｃｔｉｏｎａｎｄｕｓｅｏｆＨｇａｓｗｅｌｌａｓｔｈｅｃｏｍｂｕｓｔｉｏｎｏｆｆｏｓｓｉｌｆｕｅｌｓ(Ｎｒｉ…     

温度对氨法脱硫率影响的实验研究

对使用氨（NH3）脱除烟气中气态污染物的技术进行了分析和总结，认为氨洗涤法洗涤净化烟气是一种很有前景的方法，并就温度对SO2脱除率的影响进行了实验研究。实验研究结果显示，当温度超过54℃时，NH3对SO2仍有很高的脱除率。并根据实验结果建议，在实际氨法脱硫工程中，脱硫过程温度宜控制在60℃以下或在80℃以上。     

鞍山市双岭水泥厂污染状况调查及环境影响防治对策

通过对鞍山市双岭水泥厂污染源及周边环境的调查监测，搞清污染物的主要来源、厂区周边空气环境的质量，并评价了该厂对周边环境的影响。     

袋式除尘器在立窑烟气除尘中的应用

对立窑烟尘排放特点与立窑除尘工艺中的问题及对策进行了讨论。分析了立窑烟尘排放特征,对几种常见的立窑除尘的设备和工艺进行了比较,指出袋式除尘器可成功地用于立窑烟气除尘。并且从滤料选择、清灰方式、烟温控制、灰斗的气密性等方面详细地完善了袋式除尘器在立窑烟气除尘中的应用。     

清洁生产及其在瑞丽糖厂的实践

瑞丽糖厂从吸滤，发酵，酒精废醪液利用等方面实施清洁生产方案，从源头控制和减少污染物的产生，日排废水减少21792m^2,CODCr消减率达到85．9％，污染得到了有效控制。     

入冬水生高等植物的衰亡对河流水质的影响

上海市郊河流水体中有很高的氮、磷和有机负菏，由于受水生高等植物生灭的影响，初春河流中的氮、磷和有机负菏明显高于上一年的初冬，河流中的水生高等植物能大量地吸收水体中的氮、磷，抑制藻类生长，净化水质；但其植株残体在水中的腐解，又会重新释出营养元素，造成对水体的二次污染。在冬季，随着水生高等植物的大量死亡这种污染更加明显，应加强对水生高等植物的利用，尝试建立既能净化水质，又有创造经济效益的生态工程模式，使市郊受污水体得到资源化利用。     

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.