催化铁内电解法处理硝基苯废水的机理与动力学研究

对催化铁内电解法处理硝基苯废水降解动力学特性进行了研究。结果表明，降解过程符合准一级动力学规律。进水浓度、pH值和反应温度强烈影响硝基苯的降解速率。在实验pH值范围内，反应速率常数依次为：强酸性〉弱碱性〉弱酸性〉中性；循环伏安扫描图显示了硝基苯可以在铜电极上直接得电子还原，该反应在强酸和弱碱性条件下效果较好。反应速率常数随进水浓度的增大而减小。提高反应温度可改善处理效果，在30-45℃范围内，提高温度对处理效果的改善并不显著；当温度升高到45℃以上时，升温可以显著改善处理效果。     

Pt/MgO催化剂上NOx存储-还原反应性能

采用稀燃-富燃交替运行方式,研究存储-还原型催化剂Pt/MgO的NOx存储性能以及C3H6还原NOx反应性能.氧化存储段,NOx可被有效存储;当氧化性气氛转换为还原性气氛后,出现一个NOx峰,降低了总的转化效果.NOx峰的大小与存储段和还原段时间之比、温度等因素有关;400℃时NOx峰最小,总转化率最高.5 h循环实验表明,400℃时Pt/MgO催化剂再生良好,NOx转化率稳定在96%.于反应气氛中添加100 mg/m3SO2进行了5 h抗硫性实验,Pt/MgO催化剂的抗硫中毒能力明显强于Pt/BaO/Al2O3.     

微波解吸柠檬酸盐溶液中SO2实验研究

结合微波具有的热效应、非热效应特性，利用经改装的微波反应装置，研究了微波场下柠檬酸浓度、微波作用时间、微波功率、SO2初始浓度和搅拌速率对解吸柠檬酸盐溶液中SO2的影响，得出了影响SO2解吸率的基本规律和最佳解吸条件，并进行了分析。     

废塑料裂解生产原料油的研究

本文对聚乙烯和聚丙烯的混合物裂解成原料油进行了研究 ,在 44 0℃条件下 ,不同比例的聚乙烯和聚丙烯被裂解。结果发现 ,聚丙烯有最高的液体回收率。几种催化剂被应用到聚丙烯的裂解过程中。裂解产品组分的构成及催化剂的选择是本研究的主要内容。通过比较几种不同催化剂的催化结果发现 ,复合催化剂有更好的催化效果。本研究为将来的废塑料综合利用提供了一种新的有用方法     

固定化催化剂光反应器降解有机物研究进展

本文系统介绍了在TiO2 的非悬浆式体系中 ,光催化氧化有机污染物效率的影响因素、新型光反应器的特点以及污染物的降解动力学规律。可以预见 ,光催化氧化与传统的处理方法相比 ,有着良好的应用前景。     

Halogenated compounds and climate change: future emission levels and reduction costs

OBJECTIVES: This work assesses the contribution to climate change resulting from emissions of the group of halogenated greenhouse gases. METHODS: A bottom-up emission model covering 22 technological sectors in four major regions is described. Emission estimates for 1996 and projection for 2010 and 2020 are presented. The costs for deep cuts into projected emission levels are calculated. RESULTS: The substances covered by this study have contributed emissions of 1100 +/- 800 MT CO2 equivalents per year in 1996. In terms of their relative contribution to emissions of CO2 equivalents, this corresponds to 3 +/- 2% of global emissions of all anthropogenic greenhouse gases. The wide range of uncertainty is due to the poorly quantified net global warming potential of the ozone depleting substances, which have an indirect cooling effect on climate through the destruction of stratospheric ozone. For annual emissions of HFCs, PFCs and SF6 (which are regulated under the Kyoto Protocol and for which global warming potentials are well defined), the relative contribution is projected to increase to 2% (600 MT CO2 eq.) of global greenhouse gas emissions by 2010. This trend is expected to continue, emissions are projected to grow to a contribution of roughly 3% (870 MT CO2 eq.) in 2020 compared to 0.9% (300 MT CO2 eq.) in 1996. For HFCs, PFCs and SF6, this study identifies global emission reduction potentials of 260 MT CO2 eq. per year in 2010 and 640 MT CO2 eq. per year in 2020 at below US$ 50 per ton. These values correspond to roughly 40% and 75% of projected emissions in 2010 and 2020, respectively.     

COS,CS2 and SO2 in aluminium smelter exhaust

Measurements of carbonyl sulfide (COS) and carbondisulfide (CS₂) were carried out on samples drawn from a smoke stack of an aluminium smelter. Volume mixing ratios of 6 ppm COS and 0.1 ppm CS₂ were measured for gases from the electrolysis unit that had previously passed an Al₂O₃ fluid bed reactor and electrostatic precipitators. Specific emissions of 1.6 kg COS and 0.03 kg CS₂ per ton of primary aluminium were found. Extrapolating from this particular smelter’s conditions to a world mix specific COS emissions of about 4 kg/t(Al) are calculated resulting in emissions of annually 0.08 Tg COS into the atmosphere due to electrolytic aluminium production in 1995. Besides the photochemical conversion of anthropogenic CS₂ aluminium production is established to be the second major industrial source of COS probably exceeding automotive tire wear’s and coal combustion’s contributions.     

交通污染区城市绿化植物硫含量分布

为探讨城市绿化植物对交通环境中SO2的响应，以远离城市道路的相对清洁区公园生长的植物为对照植物，采集了广东省被广泛栽种的18种园林绿化植物的不同方位的叶片和树皮样品，用硫酸钡比浊法测定了每种植物样品在交通污染区面向机动车行驶方向、面向人行道方向及相对清洁区的植物样品等不同方位的植物叶片和树皮硫含量，分析了绿化植物在同一株植物的不同生长部位和不同环境中硫含量的分布特征。结果表明，交通污染区所有样品的叶片硫和树皮硫含量均高于相对清洁区的样品。其中，远离工厂的交通污染区生长的同一株植物，离机动车道越近，硫含量越高；靠近工厂的交通污染区的同一植物，离工厂近的部位的植物树皮硫含量高于面向机动车道一侧的植物硫含量。     

钛基燃烧催化剂的抗硫性能

本文研究了钛基非贵金属燃烧催化剂的硫中毒过程及载体吸硫特性。结果表明,催化剂的抗硫能力与载体吸硫量有关,不同催化剂的抗硫性能为:Cat.3>Cat.4>Cat.5>Cat.1>Cat.2,本文还讨论了硫中毒机理。     

活性矸对硫、氟、铬阴离子吸附的研究

本文对活性矸-硫、活性矸-氟、活性矸-铬(Ⅵ)三种吸附系统进行了研究.结果表明:活性矸静态等温吸附符合Freundlich吸附等温式;静态吸附动力学可用Bangharm吸附速率方程描述;利用Body公式可确定活性析矸-氟吸附系统的液相有效扩散系数.