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R K Tewo

R K Tewo

Tshwane University of Technology, South Africa

Title: Processing of calcium sulphide to calcium carbonate and hydrogen sulphide

Biography

Robert Kimutai Tewo has completed his Bachelor of Technology in Chemical and Process Engineering from Moi University, Kenya and he is a registered graduate chemical engineer with the Engineering Registration Board of Kenya, and currently pursuing Masters of Technology (Research) at Tshwane University of Technology, South Africa at the department of Environmental, Water and Earth Science.

Abstract

The growing problem of industrial solid waste disposal in South Africa and the rest of the world has become a subject of increasing public environmental concern. In South Africa, the neutralization of acid mine water as well as desalination processes using reverse osmosis, ion-exchange or chemical desalination, produce gypsum and metal hydroxide rich sludges. In addition, 12 000 tonnes of industrial solid gypsum waste are produced every day by the fertilizer industry in South Africa. The recent trend in the closure of landfills, as a preferred method for solid industrial waste disposal, has led to the necessity for the development of innovative ways of converting these solid wastes into usable and saleable products. The purpose of this study was to establish conditions for the chemical processing of calcium sulphide, the product of the thermal reduction of gypsum, into calcium carbonate and H2S.CaS was converted under batch conditions to soluble Ca(HS)2 by contacting it with water and H2S. In the following step the Ca(HS)2 was contacted with CO2 to precipitate CaCO3 and liberate H2S. The following findings were made: (i) CaS has a low solubility of <100 mg/l as CaS; (ii) Ca(HS)2 has a high solubility of >100 g/l (as CaS); (iii) CaCO3 with a purity of 80% was produced when the Ca(HS)2 solution was not filtered and 99% when it was filtered; (iv) the CaCO3 yield amounted to 91% and the H2S yield to 95%. The following process conditions were found to be suitable: (a) CaS concentrations in the range 100 - 300 g/l; (b) agitation speed of 125 rpm - 500 rpm, and (c) H2S feed flow-rate had no detectable effect on the dissolution of CaS; (d) CO2 flow-rate influenced the particle size and structure of the product CaCO3.

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