<style face="normal" font="default" size="100%">Data Consistency Tests Through the Use of Neural Networks and Virial Equation. Application of the Proposed Methodology to Critical Study of Density data.</style>

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<style face="normal" font="default" size="100%">Data Consistency Tests Through the Use of Neural Networks and Virial Equation. Application of the Proposed Methodology to Critical Study of Density data.</style>

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<style face="normal" font="default" size="100%">Experimental Measurement of Vapor Pressures and Densities of Pure Hexafluoropropylene. J. Chem. Eng.</style>

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<style face="normal" font="default" size="100%">Vapor-liquid equilibria of the (hexafluoroethane + 1, 1, 1 – trifluoroethane) binary system from 258 to 343 K up to 3.89 MPa. Equilibres « liquide-vapeur » du système binaire hexafluoroethane + 1, 1, 1-trifluoroethane de 258 à 343 K j</style>

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<style face="normal" font="default" size="100%">(Vapor+liquid) equilibrium data for (carbon dioxide + 1, 1-difluoroethane) system at temperatures from (258 to 343) K and pressures up to about 8 MPa</style>

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<style face="normal" font="default" size="100%">Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa. Fluid Phase Equilib</style>

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<style face="normal" font="default" size="100%">Vapor-liquid equilibrium data for the (hexafluoroethane + 1,1,1,2-tetrafluoroethane) system at temperatures from 253 to 353 K and pressures up to 4.16 Mpa.</style>

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<style face="normal" font="default" size="100%">Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa,</style>