城市垃圾焚烧中PVC环境影响研究

在城市生活垃圾中，大约有一半的氯来自PVC废物。在垃圾焚烧过程中，PVC含量的增加可导致HCl产生量的增加，并有可能成为二噁Ying生成的氯源。PVC中铅含量最高，但对生活垃圾相对贡献量不大。PVC对生活垃圾的镉相对贡献量最大，而且在含PVC垃圾焚烧过程中烟气中镉的浓度也有明显增加。此外，PVC有使重金属从底灰向飞灰转移的趋势，这对于后续的底灰处置是有利的。在分析PVC对城市垃圾焚烧过程影响的基础上，本文最后提出了结论和建议。     

钙化合物对前生体生成二英类的阻滞作用

针对城市生活垃圾焚烧（MSWI）过程中二（口恶）英类的生成机制以及焚烧飞灰的组成,研究了MSWI飞灰中常见的钙化合物（CaO,Ca（OH）2,CaCl2,CaSO4及Ca（NO3）2）对前生体五氯酚（PCP）及六氯苯（HCB）生成二（口恶）英类的阻滞作用.结果表明,280℃下加热2 h,Ca（NO3）2,Ca（OH）2和CaO对PCP生成二（口恶）英类的总阻滞效率分别为93.7%,80.4%和98.9%,而CaCl2和CaSO4几乎没有效果.CaO对PCP和HCB混合物生成二（口恶）英类物质同样具有良好的阻滞效果.另外,探讨了上述钙化合物对PCP及HCB生成二（口恶）英类的阻滞作用机理.     

脉冲电晕放电等离子体烟气脱硫技术研究

通过实验模拟烟气,观察SO_2在一种特殊的脉冲电晕放电等离子体环境中的氧化变化过程,研究了烟气温度、SO_2初始浓度等参数对SO_2氧化率、单位能量氧化量的影响规律。     

锅炉烟尘排放浓度超标成因分析及控制对策

分析了锅炉燃烧排出的危害人类健康的污染物烟尘及ＳＯ２超标的成因,以及长庆油田燃煤锅炉烟道气的监测结果。提出了控制锅炉烟尘排放浓度的对策及消烟措施。例如：推行煤炭洗选,改进燃料结构,限制烟尘超标的锅炉产品制造、安装,改进燃烧方式,强化炉内燃烧,改造除尘器。     

Comparative evaluation of processes for heavy metal removal from municipal solid waste incineration fly ash

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垃圾焚烧烟气净化和二噁英污染物的控制技术

采用焚烧法处理城市生活垃圾,在我国正得到广泛的推广应用,但焚烧也带来二噁英污染,它严重威胁着人类的健康,世界各国正在采取积极措施控制。文章介绍了二噁英的结构、性质和形成机理,从焚烧前、焚烧中、焚烧后三个方面评述了国内外近年来所发展的对二噁英污染物的控制技术。     

城市下水污泥焚烧过程中二次污染物排放特性的试验研究

在0.15 MWt循环流化床燃烧试验台上进行了城市下水污泥与煤的混烧试验,分析了烟气中的二次污染物排放特性.分析结果表明,利用循环流化床焚烧城市下水污泥时,添加辅助燃料(如煤)及改变焚烧条件,不仅可以达到稳定燃烧的目的,而且有利于抑制焚烧中二次污染物(如CO及二恶英等有机污染物)的生成.分析了焚烧污泥污染物的排放特性,为采用焚烧方式处理城市下水污泥提供了基础性试验数据.     

吸附法烟气脱硫

燃油和煤炭在燃烧过程中会产生SO2 ,这些SO2 排入大气中 ,形成酸雨 ,严重破坏生态环境 ,危害人类健康。一个世纪以来 ,人们对烟气脱硫作出了很大的努力 ,但常见的脱硫技术具有投资大、运行费用高 ,甚至有二次污染等问题。吸附法烟气脱硫工艺简单、脱硫效率高 ,是一种具有深入研究价值与应用前景的方法     

Dehalogenation Potential of Municipal Waste Incineration Fly Ash

BACKGROUND, AIMS AND SCOPE: In the first part of this paper the main principles which control the dehalogenation of polychlorinated aromatic compounds on municipal waste incineration fly ash (MWI-FA) have been discussed and the model fly ash of similar dehalogenation activity has been proposed. Even if both systems show comparable dehalogenation properties, the main question concerning the postulated identical reaction mechanism in both cases is left unanswered. The other very important point is to what extent is this dechlorination mechanism thermodynamically controlled. The same problem is often discussed in the literature also for the de novo synthetic reactions. From the data it is clear that metallic copper plays a decisive role in the mechanism of the dehalogenation reaction. Although the results reported in the first part strongly support the idea that copper acts in this dechlorination as the reaction component, in contrast to its generally accepted catalytic behaviour, we believed that additional support for this conclusion can be obtained with the help of a thermodynamic interpretation of the mechanism of the reaction. RESULTS AND DISCUSSION: The pathways of hexachlorobenzene dechlorination on MWI-FA and model fly ash were studied in a closed system at 260-300 degrees C under nitrogen atmosphere. These pathways were the same for both systems, with the following prevailing sequences: hexachlorobenzene --> pentachlorobenzene --> 1,2,3,5-tetrachlorobenzene --> 1,3,5-trichlorobenzene --> 1,3-dichlorobenzene. Thermodynamic calculations were carried out by using the method of minimization total Gibbs energy of the whole system. In the calculations, the following reaction components were taken into account: all gaseous chlorinated benzenes, benzene, hydrogen chloride, a gaseous trimer Cu3Cl3, and also Cu2O and CuCl2 as solid components. The effect of the reaction temperature and the amount of copper and water vapour were considered as well. The effect of reaction temperature was determined from the data calculated for the 500 to 750 K temperature region. The effect of the initial composition was determined for the molar amounts of copper = 0.01-3 moles and water vapour = 0.2 to 3 moles per mole of chlorobenzene isomer CONCLUSIONS: The results of hexachlorobenzene dechlorination by MWI-FA and model fly ash under comparable reaction conditions allow us to conclude that both dechlorinations proceed via the same dechlorination pathways, which can be taken as an evidence of the identical dehalogenation mechanism for both systems. The relative percentual distribution of the dehalogenated products depends on the temperature, but not on the initial amount of water vapour or copper metal. On the other hand, the initial amount of copper substantially affects the conversion of the dehalogenation as well as the molar ratio of Cu3Cl3 to HCl in the equilibrium mixture. Comparison of the experimental with thermodynamic results supports the idea that dehalogenation reactions are thermodynamically controlled. RECOMMENDATIONS AND OUTLOOK: Thermodynamic analysis of the dehalogenation reactions may prove useful for a wide range of pollutants. The calculations concerning polychlorinated biphenyls and phenols are under study.