Abstract
Sulfur dioxide expenditure – X –, moles SO2·mole−1 HNO3 –, required for reduction one mole of nitric acid at the process of product reflux by nitrogen isotopes separation by means of chemical exchange of nitrogen oxides and nitric acid was determined experimentally. Measurements were done in temperature range 283–380 K for 10.0±0.1 and 12.5 moles/l concentrations of nitric acid. For the 10 M HNO3 X changes from 1.37 ± 0.09 at 283 ± 1 K to 0.39 ± 0.07 moles SO2/mole HNO3 at 380 ± 2 K. Equilibrium model of reduction of HNO3 as well as method of calculation of X were proposed. Some data are given for the expenditure of SO2 per one mole of nitric acid and one unit of product-nitrogen-15-, when temperature changes from 283 to 380 K and nitric acid concentration changes from 6 to 15 M.