A New Process for Converting SO2 to Sulfur without Generating Secondary Pollutants through Reactions Involving CaS and CaSO4

硫黄 二氧化硫 化学 烟气脱硫 硫化氢 硫酸 硫酸盐 酸性气体 颗粒 废物管理 硫化物 无机化学 环境化学 材料科学 有机化学 工程类 复合材料
作者
Hong Yong Sohn,Byung-Su Kim
出处
期刊:Environmental Science & Technology [American Chemical Society]
卷期号:36 (13): 3020-3024 被引量:46
标识
DOI:10.1021/es011459b
摘要

Nonferrous smelters and coal gasification processes generate environmentally harmful sulfur dioxide streams, most of which are treated to produce sulfuric acid with the accompanying problems of market shortage and transportation difficulties. Some sulfur dioxide streams are scrubbed with an alkali solution or a solid substance such as limestone or dolomite, which in turn generates wastes that pose other pollution problems. While the conversion of sulfur dioxide to elemental sulfur has many environmental advantages, no processes exist that are environmentally acceptable and economically viable. A new method for converting sulfur dioxide to elemental sulfur by a cyclic process involving calcium sulfide and calcium sulfate without generating solid wastes has been developed. In this process, calcium sulfate pellets as the starting raw material are reduced by a suitable reducing agent such as hydrogen to produce calcium sulfide pellets, which are used to reduce sulfur dioxide producing elemental sulfur vapor and calcium sulfate. The latter is then reduced to regenerate calcium sulfide. Thermodynamic analysis and experimental results indicated that the CaS−SO2 reaction produces mainly sulfur vapor and solid calcium sulfate and that the gaseous product from the CaSO4−H2 reaction is mainly water vapor. The rates of the two reactions are reasonably rapid in the temperature range 1000−1100 K, and, importantly, the physical strengths and reactivities of the pellets are maintained largely unchanged up to the tenth cycle, the last cycle tested in this work. Sulfur dioxide-containing streams from certain sources, such as the regenerator off-gas from an integrated gasification combined cycle desulfurization unit and new sulfide smelting plants, contain much higher partial pressures of SO2. In these cases, the rate of the first reaction is expected to be proportionally higher than in the test conditions reported in this paper.
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