Simulation of the vapor phase composition in HNO3 – H2SO4 – H2O system with low content of nitric acid
DOI:
https://doi.org/10.15587/1729-4061.2015.55879Keywords:
mathematical modeling, HNO3 – H2SO4 – H2O system, vapor phase, composition, temperatureAbstract
Based on the analysis and processing of literature data, the mathematical model describing the vapor phase composition of the ternary system nitric acid – sulfuric acid – water from the liquid phase composition and temperature at a low mole fraction of nitric acid was developed. It was shown that even with low content of nitric acid in the system, deviations of the ideal solution and the execution of the Raoult's law to within a factor (activity coefficient), the value of which depends on the sulfuric acid concentration are observed. It was found that with an increase in the mass concentration of sulfuric acid from 60 to 80 %, the mean values of the activity coefficients increase linearly with the coefficient of determination 0, 998. The general equation of the model – dependence of the partial pressure of the nitric acid on the temperature (t, oC), the mole fraction of nitric acid (x), and the mass concentration of sulfuric acid (, % mass) has the form of a non–linear dependence, obtained by combining the Antoine, Raoult's equations and the dependence of the nitric acid activity coefficient on sulfuric acid concentration.
It was found that using the equations of the model for the ternary system HNO3 – H2SO4 – H2O at mole fraction of nitric acid in the solution of up to 0.02, it is possible to predict normal boiling points with the maximum error not exceeding 5 °C, and mole fractions of nitric acid in the vapor phase with a relative error no more than 10 %.
The model can be used as a subsystem in developing the mathematical model of the reactor for adiabatic nitration of aromatic compounds, as well as in calculating and designing the regeneration systems of spent sulfuric acid.
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