202007boubel0journalOriginalBoukais-Belaribi, G.[Ghenima]Belaribi, B. F.[Brahim Farid]Lohmann, J.[Juergen]Jose, J.[Jacques]Fluid Phase Equilib.20072008-03-05Isothermal vapour liquid equilibria and excess molar enthalpies of hex-2-yne + methyl butyl ether and hex-3-yne + dibutyl ether mixturesVapour liquid equilibriaExcess enthalpyMethyl butyl etherDibutyl etherHex-2-yneHex-3-yneThe DISQUAC modelThe modified UNIFAC (Do) model262180-1861butyl methyl etherC5H12O1Commercial source1992Stated by supplier2De-gassed by boiling or ultrasonically2992Gas chromatography2dibutyl etherC8H18O1Commercial source1992Stated by supplier2De-gassed by boiling or ultrasonically2992Gas chromatography33-hexyneC6H101Commercial source1992Stated by supplier2De-gassed by boiling or ultrasonically2992Gas chromatography42-hexyneC6H101Commercial source1992Stated by supplier2None used2992Gas chromatography11Principal objective of the workRDCTRC3/5/20081Vapor or sublimation pressure, kPaClosed cell (Static) methodLiquidDirect value, X1AuthorLiquidGas1Temperature, K1263.15513.05441.030541273.15515.43641.054361283.15519.20741.092071293.155114.9351.14931298.155118.73551.187351303.155123.30151.233011313.155135.15251.351521323.155151.45551.514551333.155173.31351.733131343.1551101.959611.0195921Principal objective of the workRDCTRC3/5/20081Vapor or sublimation pressure, kPaClosed cell (Static) methodLiquidDirect value, X1AuthorLiquidGas1Temperature, K1263.1551.07721.000771273.1551.16631.001661283.1551.33731.003371293.1551.64931.006491298.1551.88531.008851303.15511.19341.011931313.15512.10341.021031323.15513.57141.035711333.15515.86241.058621343.15519.32941.0932931Principal objective of the workRDCTRC3/5/20081Vapor or sublimation pressure, kPaClosed cell (Static) methodLiquidDirect value, X1AuthorLiquidGas1Temperature, K1263.15511.61341.032261273.15513.00141.060021283.15515.29341.105861293.15518.90941.178181298.155111.37751.227541303.155114.38851.287761313.155122.40351.448061323.155133.76651.675321333.155149.43651.988721343.155170.515511.410341Principal objective of the workRDCTRC3/5/20081Vapor or sublimation pressure, kPaClosed cell (Static) methodLiquidDirect value, X1AuthorLiquidGas1Temperature, K1263.15511.37241.027441273.15512.5641.05121283.15514.53241.090641293.15517.6641.15321298.15519.80441.196081303.155112.42851.248561313.155119.44551.38891323.155129.45651.589121333.155143.34751.866941343.155162.15511.2432131Principal objective of the workVNJCE1/4/20081Vapor or sublimation pressure, kPaClosed cell (Static) methodLiquidDirect value, X1AuthorLiquidGas1Temperature, K1Author2Mole fraction3Liquid1263.5352.233741.45231.0051273.3752.233741.84931.0051283.2752.2337411.51241.0021293.2252.2337412.59341.0021298.1852.2337413.34841.0021303.252.2337414.29341.0021313.1752.2337416.83641.0021323.1952.23374110.57151.0021333.2152.23374115.92851.0021343.2952.23374123.33551.0021353.1452.23374133.12151.0021353.1752.23374133.12851.0021293.2252.4123414.05241.0021298.252.4123415.241.0021303.252.4123416.61541.0021273.3252.4123411.3541.0021313.1752.41234110.39751.0021313.252.41234110.451.0021263.5152.412341.72931.0051323.2152.41234115.92351.0021333.2152.41234123.54451.0021283.2452.4123412.38441.0021343.1852.41234133.88251.0021343.252.41234133.88651.0021353.1452.41234147.74951.0021353.1752.41234147.75351.0021353.1452.41234147.75651.0021303.252.5479418.35841.0021263.5152.547941.93731.0051313.252.54794113.14951.0021293.252.5479415.14441.0021273.3452.5479411.7341.0021323.2152.54794119.93851.0021323.2152.54794119.93951.0021283.1952.5479413.04441.0021333.2152.54794129.3351.0021298.1852.5479416.58741.0021343.1852.54794142.00451.0021343.1852.54794142.01251.0021353.1452.54794158.73951.0021353.1452.54794158.7751.0021353.1452.54794158.78351.0021323.2152.66494123.44551.0021323.2152.66494123.44951.0021303.2252.6649419.88641.0021313.252.66494115.50351.0021293.2252.6649416.10341.0021263.5352.6649411.11941.0021333.1952.66494134.40451.0021333.2152.66494134.40451.0021333.2152.66494134.40551.0021283.2452.6649413.61541.0021298.2252.6649417.80541.0021343.1852.66494149.13151.0021343.1852.66494149.13551.0021343.1852.66494149.13651.0021343.1852.66494149.13751.0021273.3252.6649412.05541.0021353.1452.66494168.52251.0021298.252.7549418.73441.0021273.3452.7549412.3141.0021333.2152.75494138.32451.0021283.2752.7549414.05641.0021313.1752.75494117.31851.0021343.1852.75494154.65251.0021343.1852.75494154.65251.0021263.4552.7549411.25241.0021303.2252.75494111.05551.0021323.2152.75494126.16151.0021293.1752.7549416.83841.0021353.1452.75494176.09451.0021353.1452.75494176.11451.0022131Principal objective of the workVNJCE1/4/20081Excess molar enthalpy (molar enthalpy of mixing), kJ/molFlow calorimetryLiquidDirect value, X1AuthorLiquidTemperature, K298.155AuthorStandard deviation of a single value (unbiased) 0.02 1Pressure, kPa101.341Mole fraction3Liquid1Author1.159941.0421.0051.275641.0621.0051.398941.07321.0051.49641.07721.0051.578141.07621.0051.657941.06821.0051.747541.05721.0051.878341.03521.0051141Principal objective of the workVNJCE1/4/20081Vapor or sublimation pressure, kPaClosed cell (Static) methodLiquidDirect value, X1AuthorLiquidGas1Temperature, K1Author2Mole fraction4Liquid1263.6352.18412.80541.0021263.6352.18412.80241.0021273.6152.18415.01541.0021273.6152.18415.01741.0021283.5952.18418.54841.0021283.652.18418.55541.0021293.5852.184113.88951.0021298.5352.184117.4251.0021303.4552.184121.65151.0021303.4552.184121.65251.0021313.3952.184132.72551.0021313.3952.184132.72851.0021323.2652.184147.85551.0021323.2852.184147.8651.0021333.2252.184168.24451.0021333.2252.184168.23551.0021343.1152.184194.86451.0021343.1152.184194.85951.0021343.1352.184194.89351.0021263.6252.3519412.52641.0021263.6352.3519412.52741.0021273.5952.3519414.53841.0021273.652.3519414.54141.0021283.652.3519417.74941.0021293.5852.35194112.6351.0021298.5352.35194115.85451.0021298.5352.35194115.85651.0021303.4552.35194119.72751.0021303.4652.35194119.72451.0021313.452.35194129.9351.0021313.4152.35194129.93351.0021323.2952.35194143.91151.0021333.2552.35194162.85451.0021333.2652.35194162.86951.0021343.1552.35194188.04551.0021263.5952.373412.47741.0021273.5852.373414.46341.0021273.5852.373414.4641.0021283.5752.373417.63741.0021293.5552.3734112.45651.0021298.5352.3734115.64851.0021303.4652.3734119.64251.0021313.3952.3734129.55851.0021313.452.3734129.56251.0021323.2752.3734143.39251.0021323.2752.3734143.38951.0021333.2452.3734162.22651.0021333.2552.3734162.22351.0021343.1252.3734186.99851.0021263.6252.5262412.22341.0021273.652.5262413.99941.0021283.5952.5262416.87341.0021283.5952.5262416.87241.0021293.5852.52624111.28951.0021298.5252.52624114.21951.0021303.4652.52624117.74651.0021303.4752.52624117.74651.0021313.3952.52624127.04251.0021313.452.52624127.04151.0021323.2852.52624139.89751.0021323.2852.52624139.89651.0021333.2552.52624157.45451.0021333.2552.52624157.46651.0021343.1552.52624181.10851.0021263.6252.597412.10641.0021273.652.597413.79941.0021273.6152.597413.80141.0021283.5952.597416.5241.0021293.5852.5974110.72151.0021293.5852.5974110.72851.0021298.5552.5974113.53451.0021298.5652.5974113.53451.0021303.4952.5974116.91151.0021303.4952.5974116.9151.0021313.4152.5974125.80751.0021313.4152.5974125.81151.0021323.3152.5974138.19451.0021323.3152.5974138.19351.0021333.2552.5974155.20451.0021333.2552.5974155.2151.0021343.1652.5974178.13751.0021263.5152.7088411.86741.0021273.6152.7088413.42741.0021283.5952.7088415.95241.0021293.5552.7088419.8641.0021298.552.70884112.48351.0021303.4452.70884115.62551.0021313.3452.70884123.94851.0021313.3452.70884123.94751.0021323.2252.70884135.64751.0021323.2252.70884135.64651.0021333.1652.70884151.94651.0021333.1652.70884151.97251.0021333.1652.70884151.98151.0021141Principal objective of the workVNJCE1/4/20081Excess molar enthalpy (molar enthalpy of mixing), kJ/molFlow calorimetryLiquidDirect value, X1AuthorLiquidTemperature, K298.155AuthorStandard deviation of a single value (unbiased) 0.02 1Pressure, kPa101.341Mole fraction4Liquid1Author1.146841-.0621.0051.305841-.1231.0051.494941-.16331.0051.63741-.1631.0051.748941-.1431.0051.844441-.0821.005