Mixture of Isopropyl Alcohol + Glycerin

Datasets

1. P_vap - Vapor or sublimation pressure, kPa (2)
2. ρ_l - Mass density, kg/m3 (2)
3. γ - Surface tension liquid-gas, N/m (2)
4. T_boil - Boiling temperature at pressure P, K (4)

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.15	0.0986	9.33
333.15	0.2015	16.13
333.15	0.3017	19.73
333.15	0.3999	22.66
333.15	0.4998	26.66
333.15	0.5998	28.66
333.15	0.6995	30.66
333.15	0.7993	33.33
333.15	0.9024	34.93
333.15	1.0000	38.84
343.15	0.0986	10.67
343.15	0.2015	18.67
343.15	0.3017	25.33
343.15	0.3999	30.40
343.15	0.4998	35.66
343.15	0.5998	39.93
343.15	0.6995	46.66
343.15	0.7993	50.66
343.15	0.9024	56.00
343.15	1.0000	60.75

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.15	0.0986	9.33
333.15	0.2015	16.13
333.15	0.3017	19.73
333.15	0.3999	22.66
333.15	0.4998	26.66
333.15	0.5998	28.66
333.15	0.6995	30.66
333.15	0.7993	33.33
333.15	0.9024	34.93
333.15	1.0000	38.84
343.15	0.0986	10.67
343.15	0.2015	18.67
343.15	0.3017	25.33
343.15	0.3999	30.40
343.15	0.4998	35.66
343.15	0.5998	39.93
343.15	0.6995	46.66
343.15	0.7993	50.66
343.15	0.9024	56.00
343.15	1.0000	60.75

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Glycerin (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	780.6
298.15	0.0676	813.5
298.15	0.1402	848.6
298.15	0.2185	887.5
298.15	0.3031	929.1
298.15	0.3949	974.3
298.15	0.4946	1023.8
298.15	0.6036	1077.0
298.15	0.7230	1135.2
298.15	0.8545	1196.5
298.15	1.0000	1258.9
303.15	0.0000	776.6
303.15	0.0676	809.5
303.15	0.1402	844.7
303.15	0.2185	883.8
303.15	0.3031	926.4
303.15	0.3949	970.6
303.15	0.4946	1020.0
303.15	0.6036	1073.4
303.15	0.7230	1131.9
303.15	0.8545	1193.4
303.15	1.0000	1255.6
308.15	0.0000	772.3
308.15	0.0676	805.5
308.15	0.1402	840.5
308.15	0.2185	879.9
308.15	0.3031	922.3
308.15	0.3949	967.3
308.15	0.4946	1016.2
308.15	0.6036	1070.4
308.15	0.7230	1128.5
308.15	0.8545	1190.0
308.15	1.0000	1252.7
313.15	0.0000	767.9
313.15	0.0676	801.4
313.15	0.1402	836.1
313.15	0.2185	875.9
313.15	0.3031	918.4
313.15	0.3949	963.4
313.15	0.4946	1012.6
313.15	0.6036	1067.0
313.15	0.7230	1125.0
313.15	0.8545	1186.8
313.15	1.0000	1249.5
318.15	0.0000	763.3
318.15	0.0676	796.8
318.15	0.1402	831.9
318.15	0.2185	871.7
318.15	0.3031	914.5
318.15	0.3949	959.2
318.15	0.4946	1008.7
318.15	0.6036	1063.1
318.15	0.7230	1121.3
318.15	0.8545	1183.2
318.15	1.0000	1246.2
323.15	0.0000	758.6
323.15	0.0676	792.2
323.15	0.1402	827.6
323.15	0.2185	867.4
323.15	0.3031	910.2
323.15	0.3949	955.3
323.15	0.4946	1004.8
323.15	0.6036	1059.6
323.15	0.7230	1117.6
323.15	0.8545	1180.3
323.15	1.0000	1242.9
328.15	0.0000	753.8
328.15	0.0676	787.5
328.15	0.1402	823.3
328.15	0.2185	863.3
328.15	0.3031	906.2
328.15	0.3949	951.3
328.15	0.4946	1000.9
328.15	0.6036	1055.7
328.15	0.7230	1114.1
328.15	0.8545	1176.6
328.15	1.0000	1239.6
333.15	0.0000	748.9
333.15	0.0676	782.9
333.15	0.1402	818.4
333.15	0.2185	858.8
333.15	0.3031	901.6
333.15	0.3949	947.5
333.15	0.4946	997.2
333.15	0.6036	1051.9
333.15	0.7230	1110.5
333.15	0.8545	1173.1
333.15	1.0000	1236.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Glycerin (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	780.6
298.15	0.0676	813.5
298.15	0.1402	848.6
298.15	0.2185	887.5
298.15	0.3031	929.1
298.15	0.3949	974.3
298.15	0.4946	1023.8
298.15	0.6036	1077.0
298.15	0.7230	1135.2
298.15	0.8545	1196.5
298.15	1.0000	1258.9
303.15	0.0000	776.6
303.15	0.0676	809.5
303.15	0.1402	844.7
303.15	0.2185	883.8
303.15	0.3031	926.4
303.15	0.3949	970.6
303.15	0.4946	1020.0
303.15	0.6036	1073.4
303.15	0.7230	1131.9
303.15	0.8545	1193.4
303.15	1.0000	1255.6
308.15	0.0000	772.3
308.15	0.0676	805.5
308.15	0.1402	840.5
308.15	0.2185	879.9
308.15	0.3031	922.3
308.15	0.3949	967.3
308.15	0.4946	1016.2
308.15	0.6036	1070.4
308.15	0.7230	1128.5
308.15	0.8545	1190.0
308.15	1.0000	1252.7
313.15	0.0000	767.9
313.15	0.0676	801.4
313.15	0.1402	836.1
313.15	0.2185	875.9
313.15	0.3031	918.4
313.15	0.3949	963.4
313.15	0.4946	1012.6
313.15	0.6036	1067.0
313.15	0.7230	1125.0
313.15	0.8545	1186.8
313.15	1.0000	1249.5
318.15	0.0000	763.3
318.15	0.0676	796.8
318.15	0.1402	831.9
318.15	0.2185	871.7
318.15	0.3031	914.5
318.15	0.3949	959.2
318.15	0.4946	1008.7
318.15	0.6036	1063.1
318.15	0.7230	1121.3
318.15	0.8545	1183.2
318.15	1.0000	1246.2
323.15	0.0000	758.6
323.15	0.0676	792.2
323.15	0.1402	827.6
323.15	0.2185	867.4
323.15	0.3031	910.2
323.15	0.3949	955.3
323.15	0.4946	1004.8
323.15	0.6036	1059.6
323.15	0.7230	1117.6
323.15	0.8545	1180.3
323.15	1.0000	1242.9
328.15	0.0000	753.8
328.15	0.0676	787.5
328.15	0.1402	823.3
328.15	0.2185	863.3
328.15	0.3031	906.2
328.15	0.3949	951.3
328.15	0.4946	1000.9
328.15	0.6036	1055.7
328.15	0.7230	1114.1
328.15	0.8545	1176.6
328.15	1.0000	1239.6
333.15	0.0000	748.9
333.15	0.0676	782.9
333.15	0.1402	818.4
333.15	0.2185	858.8
333.15	0.3031	901.6
333.15	0.3949	947.5
333.15	0.4946	997.2
333.15	0.6036	1051.9
333.15	0.7230	1110.5
333.15	0.8545	1173.1
333.15	1.0000	1236.0

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.20	0.0000	0.0631
293.20	0.1000	0.0457
293.20	0.2000	0.0343
293.20	0.3000	0.0288
293.20	0.4000	0.0267
293.20	0.5000	0.0256
293.20	0.6000	0.0248
293.20	0.7000	0.0239
293.20	0.8000	0.0228
293.20	0.9000	0.0219
293.20	1.0000	0.0214
303.20	0.0000	0.0624
303.20	0.1000	0.0451
303.20	0.2000	0.0340
303.20	0.3000	0.0285
303.20	0.4000	0.0262
303.20	0.5000	0.0251
303.20	0.6000	0.0242
303.20	0.7000	0.0234
303.20	0.8000	0.0223
303.20	0.9000	0.0214
303.20	1.0000	0.0207
313.20	0.0000	0.0620
313.20	0.1000	0.0444
313.20	0.2000	0.0336
313.20	0.3000	0.0280
313.20	0.4000	0.0258
313.20	0.5000	0.0246
313.20	0.6000	0.0237
313.20	0.7000	0.0230
313.20	0.8000	0.0218
313.20	0.9000	0.0209
313.20	1.0000	0.0197
323.20	0.0000	0.0611
323.20	0.1000	0.0439
323.20	0.2000	0.0329
323.20	0.3000	0.0276
323.20	0.4000	0.0255
323.20	0.5000	0.0241
323.20	0.6000	0.0235
323.20	0.7000	0.0225
323.20	0.8000	0.0212
323.20	0.9000	0.0200
323.20	1.0000	0.0187
333.20	0.0000	0.0605
333.20	0.1000	0.0432
333.20	0.2000	0.0322
333.20	0.3000	0.0272
333.20	0.4000	0.0250
333.20	0.5000	0.0237
333.20	0.6000	0.0226
333.20	0.7000	0.0221
333.20	0.8000	0.0206
333.20	0.9000	0.0191
333.20	1.0000	0.0176

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Isopropyl Alcohol (1) - Liquid	Surface tension liquid-gas, N/m - Liquid
293.20	0.0000	0.0631
293.20	0.1000	0.0457
293.20	0.2000	0.0343
293.20	0.3000	0.0288
293.20	0.4000	0.0267
293.20	0.5000	0.0256
293.20	0.6000	0.0248
293.20	0.7000	0.0239
293.20	0.8000	0.0228
293.20	0.9000	0.0219
293.20	1.0000	0.0214
303.20	0.0000	0.0624
303.20	0.1000	0.0451
303.20	0.2000	0.0340
303.20	0.3000	0.0285
303.20	0.4000	0.0262
303.20	0.5000	0.0251
303.20	0.6000	0.0242
303.20	0.7000	0.0234
303.20	0.8000	0.0223
303.20	0.9000	0.0214
303.20	1.0000	0.0207
313.20	0.0000	0.0620
313.20	0.1000	0.0444
313.20	0.2000	0.0336
313.20	0.3000	0.0280
313.20	0.4000	0.0258
313.20	0.5000	0.0246
313.20	0.6000	0.0237
313.20	0.7000	0.0230
313.20	0.8000	0.0218
313.20	0.9000	0.0209
313.20	1.0000	0.0197
323.20	0.0000	0.0611
323.20	0.1000	0.0439
323.20	0.2000	0.0329
323.20	0.3000	0.0276
323.20	0.4000	0.0255
323.20	0.5000	0.0241
323.20	0.6000	0.0235
323.20	0.7000	0.0225
323.20	0.8000	0.0212
323.20	0.9000	0.0200
323.20	1.0000	0.0187
333.20	0.0000	0.0605
333.20	0.1000	0.0432
333.20	0.2000	0.0322
333.20	0.3000	0.0272
333.20	0.4000	0.0250
333.20	0.5000	0.0237
333.20	0.6000	0.0226
333.20	0.7000	0.0221
333.20	0.8000	0.0206
333.20	0.9000	0.0191
333.20	1.0000	0.0176

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0064	468.93
0.0079	459.08
0.0222	443.27
0.0293	425.27
0.0405	415.17
0.0503	404.17
0.0777	395.31
0.0980	389.81
0.1297	385.01
0.1478	380.51
0.1821	377.96
0.2106	375.56
0.2252	373.96
0.2492	373.06
0.2787	371.56
0.2915	370.71
0.3121	370.01
0.3189	369.81
0.3347	369.11
0.3580	368.41

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Gas	Mole fraction of Isopropyl Alcohol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
53.33	0.0000	539.13
53.33	0.0839	341.00
53.33	0.1685	340.50
53.33	0.1928	340.35
53.33	0.3028	340.10
53.33	0.3644	339.95
53.33	0.4015	339.90
53.33	0.4512	339.80
53.33	0.5011	339.68
53.33	0.5512	339.60
53.33	0.6522	339.55
53.33	0.7455	339.45
53.33	0.8441	339.25
53.33	0.8958	339.35
53.33	0.9218	339.46
53.33	0.9478	339.56
53.33	0.9638	339.52
53.33	0.9739	339.89
53.33	1.0000	340.05
66.66	0.0000	547.20
66.66	0.0239	346.65
66.66	0.0719	345.68
66.66	0.0839	345.36
66.66	0.1685	345.15
66.66	0.2538	345.05
66.66	0.3644	344.90
66.66	0.5011	344.70
66.66	0.5512	344.65
66.66	0.6522	344.60
66.66	0.7455	344.57
66.66	0.8441	344.50
66.66	0.8958	344.62
66.66	0.9218	344.65
66.66	0.9478	344.70
66.66	0.9638	344.75
66.66	0.9739	344.85
66.66	1.0000	345.25
79.99	0.0000	554.05
79.99	0.0839	351.02
79.99	0.0948	349.75
79.99	0.1685	349.45
79.99	0.2538	349.25
79.99	0.3644	349.09
79.99	0.4512	348.97
79.99	0.5011	348.91
79.99	0.5512	348.87
79.99	0.6522	348.83
79.99	0.7455	348.80
79.99	0.8441	348.83
79.99	0.8958	348.93
79.99	0.9218	349.01
79.99	0.9478	349.06
79.99	0.9739	349.15
79.99	1.0000	349.50
94.93	0.0000	560.68
94.93	0.0839	354.84
94.93	0.1685	354.09
94.93	0.2538	353.80
94.93	0.3644	353.65
94.93	0.4512	353.45
94.93	0.5011	353.30
94.93	0.5512	353.15
94.93	0.5890	353.05
94.93	0.6522	353.19
94.93	0.7031	353.30
94.93	0.7455	353.35
94.93	0.8441	353.45
94.93	0.8958	353.52
94.93	0.9218	353.52
94.93	0.9478	353.61
94.93	0.9739	353.75
94.93	1.0000	354.50

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Mole fraction of Isopropyl Alcohol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0064	468.93
0.0079	459.08
0.0222	443.27
0.0293	425.27
0.0405	415.17
0.0503	404.17
0.0777	395.31
0.0980	389.81
0.1297	385.01
0.1478	380.51
0.1821	377.96
0.2106	375.56
0.2252	373.96
0.2492	373.06
0.2787	371.56
0.2915	370.71
0.3121	370.01
0.3189	369.81
0.3347	369.11
0.3580	368.41

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Pressure, kPa - Gas	Mole fraction of Isopropyl Alcohol (1) - Liquid	Boiling temperature at pressure P, K - Liquid
53.33	0.0000	539.13
53.33	0.0839	341.00
53.33	0.1685	340.50
53.33	0.1928	340.35
53.33	0.3028	340.10
53.33	0.3644	339.95
53.33	0.4015	339.90
53.33	0.4512	339.80
53.33	0.5011	339.68
53.33	0.5512	339.60
53.33	0.6522	339.55
53.33	0.7455	339.45
53.33	0.8441	339.25
53.33	0.8958	339.35
53.33	0.9218	339.46
53.33	0.9478	339.56
53.33	0.9638	339.52
53.33	0.9739	339.89
53.33	1.0000	340.05
66.66	0.0000	547.20
66.66	0.0239	346.65
66.66	0.0719	345.68
66.66	0.0839	345.36
66.66	0.1685	345.15
66.66	0.2538	345.05
66.66	0.3644	344.90
66.66	0.5011	344.70
66.66	0.5512	344.65
66.66	0.6522	344.60
66.66	0.7455	344.57
66.66	0.8441	344.50
66.66	0.8958	344.62
66.66	0.9218	344.65
66.66	0.9478	344.70
66.66	0.9638	344.75
66.66	0.9739	344.85
66.66	1.0000	345.25
79.99	0.0000	554.05
79.99	0.0839	351.02
79.99	0.0948	349.75
79.99	0.1685	349.45
79.99	0.2538	349.25
79.99	0.3644	349.09
79.99	0.4512	348.97
79.99	0.5011	348.91
79.99	0.5512	348.87
79.99	0.6522	348.83
79.99	0.7455	348.80
79.99	0.8441	348.83
79.99	0.8958	348.93
79.99	0.9218	349.01
79.99	0.9478	349.06
79.99	0.9739	349.15
79.99	1.0000	349.50
94.93	0.0000	560.68
94.93	0.0839	354.84
94.93	0.1685	354.09
94.93	0.2538	353.80
94.93	0.3644	353.65
94.93	0.4512	353.45
94.93	0.5011	353.30
94.93	0.5512	353.15
94.93	0.5890	353.05
94.93	0.6522	353.19
94.93	0.7031	353.30
94.93	0.7455	353.35
94.93	0.8441	353.45
94.93	0.8958	353.52
94.93	0.9218	353.52
94.93	0.9478	353.61
94.93	0.9739	353.75
94.93	1.0000	354.50

Sources

• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• Experimental vapour - liquid equilibrium data of the quaternary system Methanol (1) + Isopropyl Alcohol (2) + Water (3) + Glycerol (4) along with Isopropyl Alcohol (2) + Glycerol (4) and Isopropyl Alcohol (2) + Water (3) binary data at atmospheric and sub-atmospheric pressures.
• Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
• Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures
• Isothermal Vapor Liquid Equilibrium of Ethanol + Glycerol and 2-Propanol + Glycerol at Different Temperatures