Abstract
A mole fraction-based multicomponent thermodynamic model, previously applied to the system H2OH2SO4, is here extended to mixtures with (NH4)2SO4 at 298.15 K. Model parameters are determined by fitting to vapour pressure data (from isopiestic and electrodynamic balance studies), together with degrees of dissociation of the bisulphate ion and salt solubilities (solid phases (NH4)2SO4, (NH4)3H(SO4)2 and NH4HSO4). The model successfully represents the thermodynamic properties of the system to high supersaturation over the full range of composition from (NH4)2SO4H2O to H2SO4H2O. Equilibrium vapour pressures of NH3 have been calculated for mixtures of various compositions. © 1995.
| Original language | English |
|---|---|
| Pages (from-to) | 19-38 |
| Journal | Journal of Aerosol Science |
| Volume | 26 |
| Issue number | 1 |
| DOIs | |
| Publication status | Published - Jan 1995 |
| Externally published | Yes |
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