CONTROL, PROBATION, AUTOMATIZATION, SIMULATION | |
ArticleName | Technique of calculation of sulphuric acid discharge by pyrometallurgical devices of industrial enterprises of Polar Division of MMC Norilsk Nickel |
ArticleAuthor | Vasilev Yu. V., Tsemekhman L. Sh., Severilov A. V., Tolstikova T. P., Chetverikov O. N. |
ArticleAuthorData | Gipronickel Institute Ltd Yu. V. Vasilev, Senior Research Officer, Laboratory of Pyrometallurgy
MMC Norilsk Nickel
Copper Plant of MMC Norilsk Nickel |
Abstract | 1. Mathematical model of sulphur anhydride oxidation to sulphuric anhydride subsequently followed by sulphuric acid formation based on pyrometallurgical process off-gases has been developed. The calculated results have been tested using on-site instrument studies carried out at three operations, namely: Nickel, Copper and Nadezhda Plants of MMC Norilsk Nickel. The principal equation has been drawn considering SO3 formation balance on catalytically active surfaces of the dust particles and flue duct’ walls and SO3 off-take from thereof at the expense of diffusion. The equation is modified into the regular differential equation of the 1st order relative to SO3 mole concentration, the duration of the gas passing from the pyrometallurgical unit to the discussed flue duct section being the said equation argument. Stoichiometry behaviour, as well as equations of material balances of sulphur, oxygen and neutral components are used as summarising data. Computational solution has been realised using the developed computer programme in Turbo Basic. The calculations have allowed specifying the temperature range important for SO2 conversion in the discussed conditions, namely narrowing it, in the majority of cases, up to 600–850 оС. Effect of the flue duct’ or the pyrometallurgical unit’ wall as a catalyst in the course of SO2 conversion has been specified, and the effect factor has been drawn. The input data set required for performing calculations due to the model has been defined. Limitations that take place in SO2 transition to SO3 and result in the relatively narrow range of changes occurring in SO2 conversion rate under the discussed conditions (mainly, 1% through 10%) have been analysed. It has been proved by the calculation results, as well as by the measured actual conversion rates. |
keywords | Sulphur anhydride, sulphuric anhydride, sulphuric acid, conversion, catalyst, diffusion, mass exchange |
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