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141.
采用不锈钢多针作为高压电极系统,水膜为低压电极.负直流高压电源供电,含二氧化硫(SO2)的污染气体从高压电极系统的轴向进入,沿着电晕放电电场从水膜上方通过,在电晕放电等离子体和水吸收共同作用下,生成硫酸使SO2得到脱除.主要研究了放电电压、气体中SO2初始浓度和气体在电极系统的停留时间对脱硫效果的影响,并测试了水中SO32-和SI42-离子浓度,分析SO2脱除机制.结果表明,电晕放电和水吸收对SO2脱除具有很好的协同作用,脱硫效果明显升高,SO2转变生成硫酸量的体积分数提高;脱硫效果随电压增加和停留时间的增加而增加,初始浓度对脱硫效果有影响.当SO2初始浓度(体积分数)为430×10-6,施加电压为14.5 kV,停留时间为7.5 s时,脱硫效率达90%以上. 相似文献
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143.
The present paper deals with the location of tanks in a tank farm, in chemical and allied industries. Ideally the tanks are so placed and installed that in case of fire, the neighbouring tanks could remain safe. The safe distance of separation among the tanks is calculated in no wind condition, as well as, in the presence of wind. The paper uses the methods available in literature and modifies the point source model to include the effect of wind vector on the flame height during the calculation of safe inter-tank distance. It is found that for wind velocity > 4 m/s, the modified point source model provides appropriate inter-tank distance. However, for no wind and with wind velocity < 4 m/s, the Shokri-Beyler’s method provides safe inter-tank distance. 相似文献
144.
79Se是高放废物地质处置安全评价中的重点关注的核素之一,如何有效地阻滞其在处置库环境中的迁移扩散是目前研究的热点。将金属盐溶液和有机溶剂与水滑石和膨润土混合制备,分别得到2种无机改性水滑石和9种不同的有机和无机改性膨润土,通过批次实验研究这些改性材料对Se(IV)的吸附性能。结果表明无机改性的水滑石和膨润土对Se(IV)均有较好的吸附,吸附率超过57%。而有机改性的膨润土吸附效果很差,吸附率低于10%。采用SEM和XRD对这些改性材料进行表征,结果表明:无机改性后的膨润土的比表面积和层间距均增大,有利于对Se(IV)的吸附。 相似文献
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Despite the extensive use of sulfur in the industry, very little information is available in the literature on its key dust explosion properties. The work presented in this paper contributes to filling the current knowledge gaps on sulfur dust explosion properties and focuses on the experimental determination of the MEC of sulfur dust using a Modified Hartmann Tube and a 20 L dust explosion sphere. First, the MEC of sulfur dust samples collected at a sulfur production facility from areas prone to the generation of fine sulfur dust was measured. The results showed that these sulfur dust samples are fine enough to cause dust explosions with 55 ± 5< MEC <105 ± 5 g/m3. Second, the influence of the particle size of sulfur dust was investigated with both equipment. The use of the Modified Hartmann Tube for MEC determination showed that the MEC increases with increasing particle size in the particle size range of 0–2000 μm. Unlike the Modified Hartmann Tube, MEC experiments done in the 20 L Sphere did not allow the quantification of the influence of the particle size on the MEC. These results were explained by the phenomenon of particle breakage induced by the 20 L Sphere's dispersion mechanism. Additional experiments with the 20 L sphere confirmed the particle breakage of sulfur dust particles and showed that it is inversely proportional to dust concentration and proportional to the dust's original particle size distribution. 相似文献
147.