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CONTROL, PROBATION, AUTOMATIZATION, SIMULATION
Название Technique of calculation of sulphuric acid discharge by pyrometallurgical devices of industrial enterprises of Polar Division of MMC Norilsk Nickel
Автор Vasilev Yu. V., Tsemekhman L. Sh., Severilov A. V., Tolstikova T. P., Chetverikov O. N.
Информация об авторе

Gipronickel Institute Ltd

Yu. V. Vasilev, Senior Research Officer, Laboratory of Pyrometallurgy
L. Sh. Tsemekhman, Head of Laboratory of Pyrometallurgy

 

MMC Norilsk Nickel
A. V. Severilov, Chief Manager, Forward Development Department

 

Copper Plant of MMC Norilsk Nickel
T. P. Tolstikova, Chief Specialist
O. N. Chetverikov, Principal Processing Engineer, Laboratory of Scientific Maintenance of Production

Реферат

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.
2.Results of inspection have been processed based on the empirical coefficients enabling to create the simplified method for calculating amount of SO3 and Н2SO4 condensate generated in the flue ducts.

Ключевые слова Sulphur anhydride, sulphuric anhydride, sulphuric acid, conversion, catalyst, diffusion, mass exchange
Библиографический список

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