V. Torretta, M. Schiavon, E. Papa, P. Caruson, A. Capodaglio
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引用次数: 6
摘要
在位于突尼斯Skhira的一家磷酸厂的生产线上安装了一个处理含硫恶臭气体的试验工厂。空气污染控制系统由第一级组成,包括一个化学洗涤器,使用含有苛性钠的碱性溶液,然后是一个两级生物滴滤器(BTF),填充贻贝壳。研究了双级BTF对磷酸反应器排气中硫化氢(H2S)、二氧化硫(SO2)和二甲基硫化物(DMS)的去除效果。二级BTF进口H2S、SO2和DMS浓度分别为10 ~ 30 ppm、< 1 ~ 20 ppm和16 ~ 30 ppm。除第一天出水的H2S浓度(10 ppm)外,其余各生物步骤出水浓度均< 1 ppm。所有化合物的去除率一般都在95%以上,并且即使废气流量增加也保持较高的去除率。对H2S、SO2和DMS的质量去除率分别至少为2.0 g m-3 h-1、0.5 g m-3 h-1和6.2 g m-3 h-1。由于使用了高质量的原磷酸盐,该工艺的去除效率令人满意,特别是考虑到入口浓度已经很低。
Removal of odorous sulphur compounds from industrial gases by biotrickling filters
A pilot plant for the treatment of Sulphur-based odorous gases was installed in a line of a phosphoric acid plant located in Skhira, Tunisia. The air pollution control system train consisted of a first stage, including a chemical scrubber operating with an alkaline solution containing caustic soda, followed by a two-stage biotrickling filter (BTF) filled with Mytilus edulis shells. This study evaluated the performance of the dual-stage BTF in removing hydrogen sulphide (H2S), sulphur dioxide (SO2) and dimethyl sulphide (DMS) from the phosphoric acid reactor's exhaust air current. Concentrations of H2S, SO2 and DMS at the inlet of the two-stage BTF were 10-30 ppm, < 1-20 ppm and 16-30 ppm, respectively. All of the respective concentrations at the outlet of the biological step were < 1 ppm, except for the H2S in the outlet during the first day of operation (10 ppm). Removal efficiencies were generally higher than 95% for all compounds, and remained high even with an increase of the off-gas flow rate. Mass-removal capacity was at least 2.0 g m-3 h-1, 0.5 g m-3 h-1 and 6.2 g m-3 h-1, for H2S, SO2 and DMS, respectively. The removal efficiencies of the process were satisfactory, especially considering the already low inlet concentrations, due to the high quality of the raw phosphate used.