Fugacity ratio estimations for high-melting rigid aromatic compounds.
Prediction of the environmental fate of organic compounds requires knowledge of their tendency to stay in the gas and water phase. Vapor pressure and aqueous solubility are commonly used descriptors for these processes. Depending on the type of distribution process, values for either the pure solid state or the (subcooled) liquid state have to be used. Values for the (subcooled) liquid state can be calculated from those for the solid state, and vice versa, using the fugacity ratio. Fugacity ratios are usually calculated from the entropy of fusion and the melting point. For polycyclic aromatic hydrocarbons, chlorobenzenes, chlorodibenzofuranes, and chlorodibenzo(p)dioxins, fugacity ratios calculated using experimental entropies of fusion were systematically less than those obtained from a thermodynamically more rigorous approach using heat capacity data. The deviation was more than 1 order of magnitude at the highest melting point. The use of a universal value for the entropy of fusion of 56 J/molK resulted in either over or underestimation by up to more than 1 order of magnitude. A simple correction factor, based on the melting point only, was derived. This correction factor allowed the fugacity ratios to be estimated from experimental entropies of fusion and melting point with an accuracy better than 0.1-0.2 log units.
Van Noort
Paul C M
PC
Institute for Inland Water Management and Wastewater Treatment (RIZA), P.O. Box 17, Lelystad 8200 AA, The Netherlands. p.vnoort@riza.rws.minvenw.nl
D001572:Benzofurans / Q000737:chemistry*; D002722:Chlorobenzenes / Q000737:chemistry*; D004147:Dioxins / Q000737:chemistry*; D019277:Entropy; D008956:Models, Chemical; D044367:Phase Transition; D011084:Polycyclic Aromatic Hydrocarbons / Q000737:chemistry*; D044366:Transition Temperature
D001572:Benzofurans; D002722:Chlorobenzenes; D004147:Dioxins; D011084:Polycyclic Aromatic Hydrocarbons