202005milpau0journalOriginalMilhet, M.Pauly, J.Coutinho, J. A. P.Dirand, M.Daridon, J. L.Fluid Phase Equilib.20052005-08-19Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems(Solid + liquid) equilibriaBinary systemn-AlkanesTetradecanePentadecaneHexadecaneHigh pressureModelling235173-1811tetradecaneC14H301Commercial source1992Stated by supplier2None used2pentadecaneC15H321Commercial source1992Stated by supplier2None used3hexadecaneC16H341Commercial source1992Stated by supplier2None used11Principal objective of the workJCEJCE8/18/20051Solid-liquid equilibrium temperature, KVisual observationCrystalDirect value, X1AuthorCrystalLiquid1Pressure, kPaAuthorStandard deviation of a single value (unbiased)110031279.241.212000051284.241.214000051289.141.216000051293.841.218000051297.941.2110000061301.741.221Principal objective of the workJCEJCE8/18/20051Solid-liquid equilibrium temperature, KVisual observationCrystalDirect value, X1AuthorCrystalLiquid1Pressure, kPaAuthorStandard deviation of a single value (unbiased)110031283.241.212000051287.841.214000051291.941.216000051296.241.218000051300.141.2110000061303.941.231Principal objective of the workJCEJCE8/18/20051Solid-liquid equilibrium temperature, KVisual observationCrystal 1Direct value, X1AuthorCrystal 1Liquid1Pressure, kPaAuthorStandard deviation of a single value (unbiased)110031291.541.21200005129641.214000051300.441.216000051304.841.218000051309.741.2110000061313.541.23111Principal objective of the workJCEJCE8/16/20051Solid-liquid equilibrium temperature, KVisual observationLiquidDirect value, X1AuthorLiquidCrystal11Pressure, kPaAuthorStandard deviation of a single value (unbiased)2Mole fraction3Liquid1Author110032001279.241.2110032.0521278.141.2110032.131277.541.2110032.1531276.741.212000052001284.241.212000052.0521282.941.212000052.131282.241.212000052.1531281.541.214000052001289.141.214000052.0521287.541.214000052.131286.741.214000052.1531285.841.216000052001293.841.216000052.0521291.841.216000052.131291.241.216000052.1531290.141.218000052001297.941.218000052.0521296.341.218000052.131295.441.218000052.1531294.141.2110000062001301.741.2110000062.0521300.441.2110000062.131299.541.2110000062.1531298.541.23111Principal objective of the workJCEJCE8/16/20051Solid-liquid equilibrium temperature, KVisual observationLiquidDirect value, X1AuthorLiquidCrystal 231Pressure, kPaAuthorStandard deviation of a single value (unbiased)2Mole fraction3Liquid1Author110032.17531276.241.212000052.17531280.341.214000052.17531284.441.216000052.17531288.241.218000052.17531291.941.2110000062.17531295.641.214000052.231284.741.216000052.231288.541.2110032.231276.541.218000052.231292.341.212000052.231280.741.2110000062.231295.941.216000052.2531289.341.2110032.253127741.212000052.2531281.341.218000052.2531292.941.214000052.2531285.441.2110000062.2531296.541.216000052.43129241.218000052.431295.841.212000052.431284.241.214000052.431288.141.2110032.431279.541.2110000062.431299.341.23111Principal objective of the workJCEJCE8/16/20051Solid-liquid equilibrium temperature, KVisual observationLiquidDirect value, X1AuthorLiquidCrystal 131Pressure, kPaAuthorStandard deviation of a single value (unbiased)2Mole fraction3Liquid1Author110032.531283.241.212000052.53128841.214000052.53129241.216000052.531296.741.218000052.531300.941.2110000062.531305.141.2110032.631285.141.212000052.631289.841.214000052.631294.141.216000052.631299.141.218000052.631303.741.2110000062.631307.441.2110032.7531288.341.212000052.753129341.214000052.7531297.441.216000052.7531301.841.218000052.7531306.341.2110000062.7531310.641.2110032.8331288.941.212000052.8331293.641.214000052.8331298.241.216000052.8331302.941.218000052.8331307.241.2110000062.8331311.441.2110032.931290.341.212000052.931295.141.214000052.931299.641.216000052.931304.141.218000052.931308.441.2110000062.931312.741.2110032141291.541.21200005214129641.214000052141300.441.216000052141304.841.218000052141309.741.2110000062141313.541.21121Principal objective of the workJCEJCE8/16/20051Solid-liquid equilibrium temperature, KVisual observationLiquidDirect value, X1AuthorLiquidCrystal11Pressure, kPaAuthorStandard deviation of a single value (unbiased)2Mole fraction2Liquid1Author110032001279.241.2110032.0521278.141.2110032.131277.441.2110032.12531277.141.2110032.1531276.241.212000052001284.241.212000052.0521282.841.212000052.131282.141.212000052.12531281.741.212000052.1531280.641.214000052001289.141.214000052.0521287.441.214000052.131286.741.214000052.12531286.441.214000052.1531284.841.216000052001293.841.216000052.0521291.941.216000052.131291.241.216000052.12531290.741.216000052.1531288.841.218000052001297.941.218000052.0521296.341.218000052.131295.541.218000052.12531294.941.218000052.1531292.741.2110000062001301.741.2110000062.0521300.441.2110000062.131299.741.2110000062.12531298.941.2110000062.1531296.341.21121Principal objective of the workJCEJCE8/16/20051Solid-liquid equilibrium temperature, KVisual observationLiquidDirect value, X1AuthorLiquidCrystal21Pressure, kPaAuthorStandard deviation of a single value (unbiased)2Mole fraction2Liquid1Author110032.231276.741.2110032.2531276.941.2110032.531278.741.2110032.7531280.841.2110032141283.241.212000052.231280.941.212000052.2531281.241.212000052.53128341.212000052.7531285.241.212000052141287.841.214000052.231285.141.214000052.2531285.341.214000052.531287.341.214000052.7531289.541.214000052141291.941.216000052.2531289.441.216000052.531291.341.216000052.7531293.541.216000052141296.241.218000052.2531293.241.218000052.531295.141.218000052.7531297.441.218000052141300.141.2110000062.2531296.941.2110000062.531298.841.2110000062.7531301.141.2110000062141303.941.216000052.231289.141.218000052.231292.941.2110000062.231296.741.2