Abstract
For the treatment of acidic waste gases, the authors selected a sparged column without internals with countercurrent gas and liquid flow. With the aim of finding the optimal process conditions, experiments were performed on the treatment of gas consisting of 40% hydrogen sulfide and 60% carbon dioxide, varying the flow rates of air, raw gas, and adsorbent, as well as the height of the upper and lower zones of the reactor. The profiles obtained for the vertical distribution of hydrogen sulfide concentration in the catalyst complex were used in developing a mathematical model of the process. On the basis of the results obtained in these studies, engineering guidelines have been developed for the design of a unit for the treatment of gas obtained in carbonation of sour caustic waste.
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