Mixture of 2-Propanol, 2-methyl- + 1,3-Dioxolane

Datasets

1. Mole fraction (2)
2. ρ_l - Mass density, kg/m3 (2)
3. c_sound,fluid - Speed of Sound, m/s (2)
4. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of 1,3-Dioxolane (2) [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (2) - Liquid	Pressure, kPa - Gas	Mole fraction of 1,3-Dioxolane (2) - Gas
0.0154	40.00	0.0439
0.0206	101.30	0.0603
0.0819	40.00	0.1869
0.1210	101.30	0.2052
0.1725	101.30	0.2643
0.1808	40.00	0.3343
0.2436	40.00	0.4144
0.2437	101.30	0.3397
0.3372	40.00	0.5048
0.3630	101.30	0.4428
0.5056	101.30	0.5627
0.5159	40.00	0.6338
0.5631	40.00	0.6607
0.5672	101.30	0.6148
0.6011	101.30	0.6319
0.6018	40.00	0.6862
0.7104	101.30	0.7243
0.7114	40.00	0.7548
0.7534	40.00	0.7846
0.7535	101.30	0.7589
0.8450	40.00	0.8787
0.8452	101.30	0.8363
0.8870	101.30	0.8749
0.8881	40.00	0.8858
0.9547	40.00	0.9486
0.9548	101.30	0.9457

Mole fraction of 1,3-Dioxolane (2) [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (2) - Liquid	Pressure, kPa - Gas	Mole fraction of 1,3-Dioxolane (2) - Gas
0.0154	40.00	0.0439
0.0206	101.30	0.0603
0.0819	40.00	0.1869
0.1210	101.30	0.2052
0.1725	101.30	0.2643
0.1808	40.00	0.3343
0.2436	40.00	0.4144
0.2437	101.30	0.3397
0.3372	40.00	0.5048
0.3630	101.30	0.4428
0.5056	101.30	0.5627
0.5159	40.00	0.6338
0.5631	40.00	0.6607
0.5672	101.30	0.6148
0.6011	101.30	0.6319
0.6018	40.00	0.6862
0.7104	101.30	0.7243
0.7114	40.00	0.7548
0.7534	40.00	0.7846
0.7535	101.30	0.7589
0.8450	40.00	0.8787
0.8452	101.30	0.8363
0.8870	101.30	0.8749
0.8881	40.00	0.8858
0.9547	40.00	0.9486
0.9548	101.30	0.9457

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0495	789.79
298.15	0.0965	798.83
298.15	0.1996	820.33
298.15	0.2909	840.96
298.15	0.4049	868.7
298.15	0.4972	892.83
298.15	0.5974	920.82
298.15	0.7033	952.73
298.15	0.8033	985.46
298.15	0.8944	1017.75
298.15	0.9439	1036.49
313.15	0.0567	775.49
313.15	0.0949	782.77
313.15	0.1973	803.78
313.15	0.2919	824.8
313.15	0.4039	851.81
313.15	0.4951	875.4
313.15	0.5948	903.12
313.15	0.6997	934.45
313.15	0.8031	967.86
313.15	0.8959	1000.17
313.15	0.9464	1018.99

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0495	789.79
298.15	0.0965	798.83
298.15	0.1996	820.33
298.15	0.2909	840.96
298.15	0.4049	868.7
298.15	0.4972	892.83
298.15	0.5974	920.82
298.15	0.7033	952.73
298.15	0.8033	985.46
298.15	0.8944	1017.75
298.15	0.9439	1036.49
313.15	0.0567	775.49
313.15	0.0949	782.77
313.15	0.1973	803.78
313.15	0.2919	824.8
313.15	0.4039	851.81
313.15	0.4951	875.4
313.15	0.5948	903.12
313.15	0.6997	934.45
313.15	0.8031	967.86
313.15	0.8959	1000.17
313.15	0.9464	1018.99

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0495	1129.2
298.15	0.0965	1135.6
298.15	0.1996	1151.0
298.15	0.2909	1165.8
298.15	0.4049	1186.2
298.15	0.4972	1204.9
298.15	0.5974	1226.8
298.15	0.7033	1252.5
298.15	0.8033	1279.3
298.15	0.8944	1305.9
298.15	0.9439	1321.3
313.15	0.0567	1065.2
313.15	0.0949	1071.1
313.15	0.1973	1087.4
313.15	0.2919	1103.5
313.15	0.4039	1123.4
313.15	0.4951	1141.2
313.15	0.5948	1162.4
313.15	0.6997	1187.1
313.15	0.8031	1213.5
313.15	0.8959	1239.6
313.15	0.9464	1254.3

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1,3-Dioxolane (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0495	1129.2
298.15	0.0965	1135.6
298.15	0.1996	1151.0
298.15	0.2909	1165.8
298.15	0.4049	1186.2
298.15	0.4972	1204.9
298.15	0.5974	1226.8
298.15	0.7033	1252.5
298.15	0.8033	1279.3
298.15	0.8944	1305.9
298.15	0.9439	1321.3
313.15	0.0567	1065.2
313.15	0.0949	1071.1
313.15	0.1973	1087.4
313.15	0.2919	1103.5
313.15	0.4039	1123.4
313.15	0.4951	1141.2
313.15	0.5948	1162.4
313.15	0.6997	1187.1
313.15	0.8031	1213.5
313.15	0.8959	1239.6
313.15	0.9464	1254.3

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0154	40.00	333.27
0.0206	101.30	354.19
0.0819	40.00	331.10
0.1210	101.30	352.15
0.1725	101.30	351.89
0.1808	40.00	328.67
0.2436	40.00	327.13
0.2437	101.30	351.02
0.3372	40.00	326.14
0.3630	101.30	349.80
0.5056	101.30	348.63
0.5159	40.00	324.39
0.5631	40.00	324.16
0.5672	101.30	348.38
0.6011	101.30	348.26
0.6018	40.00	323.78
0.7104	101.30	347.91
0.7114	40.00	323.32
0.7534	40.00	323.18
0.7535	101.30	347.88
0.8450	40.00	322.94
0.8452	101.30	347.90
0.8870	101.30	348.05
0.8881	40.00	322.95
0.9547	40.00	323.04
0.9548	101.30	348.28

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 1,3-Dioxolane (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0154	40.00	333.27
0.0206	101.30	354.19
0.0819	40.00	331.10
0.1210	101.30	352.15
0.1725	101.30	351.89
0.1808	40.00	328.67
0.2436	40.00	327.13
0.2437	101.30	351.02
0.3372	40.00	326.14
0.3630	101.30	349.80
0.5056	101.30	348.63
0.5159	40.00	324.39
0.5631	40.00	324.16
0.5672	101.30	348.38
0.6011	101.30	348.26
0.6018	40.00	323.78
0.7104	101.30	347.91
0.7114	40.00	323.32
0.7534	40.00	323.18
0.7535	101.30	347.88
0.8450	40.00	322.94
0.8452	101.30	347.90
0.8870	101.30	348.05
0.8881	40.00	322.95
0.9547	40.00	323.04
0.9548	101.30	348.28

Sources

• (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
• Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K