Mixture of 2-Propanol, 2-methyl- + Glycerin

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. n₀ - Refractive index (Na D-line) (2)
4. ρ_l - Mass density, kg/m3 (2)
5. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of 2-Propanol, 2-methyl- (1) [ref]

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Propanol, 2-methyl- (1) - Gas
0.0000	547.25	0.0000
0.0146	511.98	0.6609
0.0255	490.85	0.8357
0.0302	483.68	0.8790
0.0491	460.78	0.9535
0.0996	427.89	0.9857
0.1523	409.91	0.9904
0.2009	399.12	0.9975
0.3035	383.64	0.9993
0.4024	373.56	0.9994
0.5041	365.79	0.9996
0.6033	359.79	0.9997
0.7019	354.91	0.9998
0.8026	350.80	0.9999
0.8645	348.65	0.9999
0.9022	347.47	1.0000
0.9490	346.13	1.0000
0.9646	345.72	1.0000
0.9746	345.46	1.0000
0.9852	345.19	1.0000
1.0000	344.84	1.0000
0.0000	553.96	0.0000
0.0146	520.26	0.6247
0.0255	500.05	0.8121
0.0302	492.22	0.8497
0.0491	469.36	0.9395
0.0996	436.04	0.9832
0.1523	417.08	0.9958
0.2009	405.58	0.9970
0.3035	389.42	0.9986
0.4024	378.96	0.9990
0.5041	370.91	0.9992
0.6033	364.70	0.9994
0.7019	359.65	0.9996
0.8026	355.40	0.9998
0.8645	353.18	0.9999
0.9022	351.96	1.0000
0.9490	350.58	1.0000
0.9646	350.15	1.0000
0.9746	349.88	1.0000
0.9852	349.61	1.0000
1.0000	349.23	1.0000
0.0000	560.95	0.0000
0.0146	528.86	0.5921
0.0255	509.15	0.7851
0.0302	501.65	0.8303
0.0491	478.85	0.9365
0.0996	443.55	0.9825
0.1523	423.95	0.9906
0.2009	412.20	0.9967
0.3035	395.40	0.9986
0.4024	384.54	0.9989
0.5041	376.19	0.9990
0.6033	369.78	0.9994
0.7019	364.57	0.9996
0.8026	360.18	0.9998
0.8645	357.88	0.9998
0.9022	356.62	0.9999
0.9490	355.19	1.0000
0.9646	354.74	1.0000
0.9746	354.47	1.0000
0.9852	354.18	1.0000
1.0000	353.80	1.0000

Mole fraction of 2-Propanol, 2-methyl- (1) [ref]

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Propanol, 2-methyl- (1) - Gas
0.0000	547.25	0.0000
0.0146	511.98	0.6609
0.0255	490.85	0.8357
0.0302	483.68	0.8790
0.0491	460.78	0.9535
0.0996	427.89	0.9857
0.1523	409.91	0.9904
0.2009	399.12	0.9975
0.3035	383.64	0.9993
0.4024	373.56	0.9994
0.5041	365.79	0.9996
0.6033	359.79	0.9997
0.7019	354.91	0.9998
0.8026	350.80	0.9999
0.8645	348.65	0.9999
0.9022	347.47	1.0000
0.9490	346.13	1.0000
0.9646	345.72	1.0000
0.9746	345.46	1.0000
0.9852	345.19	1.0000
1.0000	344.84	1.0000
0.0000	553.96	0.0000
0.0146	520.26	0.6247
0.0255	500.05	0.8121
0.0302	492.22	0.8497
0.0491	469.36	0.9395
0.0996	436.04	0.9832
0.1523	417.08	0.9958
0.2009	405.58	0.9970
0.3035	389.42	0.9986
0.4024	378.96	0.9990
0.5041	370.91	0.9992
0.6033	364.70	0.9994
0.7019	359.65	0.9996
0.8026	355.40	0.9998
0.8645	353.18	0.9999
0.9022	351.96	1.0000
0.9490	350.58	1.0000
0.9646	350.15	1.0000
0.9746	349.88	1.0000
0.9852	349.61	1.0000
1.0000	349.23	1.0000
0.0000	560.95	0.0000
0.0146	528.86	0.5921
0.0255	509.15	0.7851
0.0302	501.65	0.8303
0.0491	478.85	0.9365
0.0996	443.55	0.9825
0.1523	423.95	0.9906
0.2009	412.20	0.9967
0.3035	395.40	0.9986
0.4024	384.54	0.9989
0.5041	376.19	0.9990
0.6033	369.78	0.9994
0.7019	364.57	0.9996
0.8026	360.18	0.9998
0.8645	357.88	0.9998
0.9022	356.62	0.9999
0.9490	355.19	1.0000
0.9646	354.74	1.0000
0.9746	354.47	1.0000
0.9852	354.18	1.0000
1.0000	353.80	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
423.15	0.5000	520.00
423.15	0.6000	620.00
423.15	0.7100	540.00
423.15	0.7800	630.00
423.15	0.8300	630.00
423.15	0.9100	670.00
423.15	0.9700	730.00
448.15	0.5000	820.00
448.15	0.6000	1090.00
448.15	0.7100	990.00
448.15	0.7800	1050.00
448.15	0.8300	1110.00
448.15	0.9100	1220.00
448.15	0.9700	1290.00
473.15	0.5000	1050.00
473.15	0.6000	1270.00
473.15	0.7100	1350.00
473.15	0.7800	1540.00
473.15	0.8300	1740.00
473.15	0.9100	1880.00
473.15	0.9700	2070.00
498.15	0.5000	1780.00
498.15	0.6000	2060.00
498.15	0.7100	2490.00
498.15	0.7800	2430.00
498.15	0.8300	2630.00
498.15	0.9100	2830.00
498.15	0.9700	3230.00
523.15	0.5000	3220.00
523.15	0.6000	3400.00
523.15	0.7100	3400.00
523.15	0.7800	3650.00
523.15	0.8300	3610.00
523.15	0.9100	4450.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
423.15	0.5000	520.00
423.15	0.6000	620.00
423.15	0.7100	540.00
423.15	0.7800	630.00
423.15	0.8300	630.00
423.15	0.9100	670.00
423.15	0.9700	730.00
448.15	0.5000	820.00
448.15	0.6000	1090.00
448.15	0.7100	990.00
448.15	0.7800	1050.00
448.15	0.8300	1110.00
448.15	0.9100	1220.00
448.15	0.9700	1290.00
473.15	0.5000	1050.00
473.15	0.6000	1270.00
473.15	0.7100	1350.00
473.15	0.7800	1540.00
473.15	0.8300	1740.00
473.15	0.9100	1880.00
473.15	0.9700	2070.00
498.15	0.5000	1780.00
498.15	0.6000	2060.00
498.15	0.7100	2490.00
498.15	0.7800	2430.00
498.15	0.8300	2630.00
498.15	0.9100	2830.00
498.15	0.9700	3230.00
523.15	0.5000	3220.00
523.15	0.6000	3400.00
523.15	0.7100	3400.00
523.15	0.7800	3650.00
523.15	0.8300	3610.00
523.15	0.9100	4450.00

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 95.99 (Liquid)

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
0.0000	303.15	1.4719
0.0458	303.15	1.4678
0.0955	303.15	1.4634
0.1560	303.15	1.458
0.2040	303.15	1.4538
0.2515	303.15	1.4496
0.3012	303.15	1.4451
0.3491	303.15	1.4409
0.4060	303.15	1.4359
0.4530	303.15	1.4317
0.5010	303.15	1.4275
0.5520	303.15	1.4229
0.6056	303.15	1.4182
0.6582	303.15	1.4135
0.7032	303.15	1.4095
0.7536	303.15	1.4051
0.8064	303.15	1.4004
0.8570	303.15	1.3959
0.8967	303.15	1.3924
0.9567	303.15	1.3863
1.0000	303.15	1.3822
0.0000	308.15	1.4694
0.0458	308.15	1.4653
0.0955	308.15	1.4609
0.1560	308.15	1.4554
0.2040	308.15	1.4511
0.2515	308.15	1.4469
0.3012	308.15	1.4424
0.3491	308.15	1.4382
0.4060	308.15	1.4331
0.4530	308.15	1.4288
0.5010	308.15	1.4245
0.5520	308.15	1.42
0.6056	308.15	1.4152
0.6582	308.15	1.4105
0.7032	308.15	1.4064
0.7536	308.15	1.4019
0.8064	308.15	1.3972
0.8570	308.15	1.3927
0.8967	308.15	1.389
0.9567	308.15	1.3838
1.0000	308.15	1.3803
0.0000	313.15	1.4673
0.0458	313.15	1.4631
0.0955	313.15	1.4587
0.1560	313.15	1.4532
0.2040	313.15	1.4489
0.2515	313.15	1.4446
0.3012	313.15	1.4402
0.3491	313.15	1.4359
0.4060	313.15	1.4308
0.4530	313.15	1.4265
0.5010	313.15	1.4222
0.5520	313.15	1.4176
0.6056	313.15	1.4128
0.6582	313.15	1.4081
0.7032	313.15	1.404
0.7536	313.15	1.3995
0.8064	313.15	1.3947
0.8570	313.15	1.3902
0.8967	313.15	1.3866
0.9567	313.15	1.3812
1.0000	313.15	1.3778
0.0000	318.15	1.4657
0.0458	318.15	1.4616
0.0955	318.15	1.457
0.1560	318.15	1.4515
0.2040	318.15	1.4472
0.2515	318.15	1.4429
0.3012	318.15	1.4384
0.3491	318.15	1.434
0.4060	318.15	1.4288
0.4530	318.15	1.4245
0.5010	318.15	1.4202
0.5520	318.15	1.4156
0.6056	318.15	1.4107
0.6582	318.15	1.4059
0.7032	318.15	1.4018
0.7536	318.15	1.3972
0.8064	318.15	1.3924
0.8570	318.15	1.3878
0.8967	318.15	1.3842
0.9567	318.15	1.3788
1.0000	318.15	1.3757
0.0000	323.15	1.4645
0.0458	323.15	1.4603
0.0955	323.15	1.4557
0.1560	323.15	1.4501
0.2040	323.15	1.4457
0.2515	323.15	1.4413
0.3012	323.15	1.4367
0.3491	323.15	1.4323
0.4060	323.15	1.427
0.4530	323.15	1.4227
0.5010	323.15	1.4183
0.5520	323.15	1.4136
0.6056	323.15	1.4087
0.6582	323.15	1.4038
0.7032	323.15	1.3997
0.7536	323.15	1.395
0.8064	323.15	1.3901
0.8570	323.15	1.3855
0.8967	323.15	1.3818
0.9567	323.15	1.3763
1.0000	323.15	1.3737
0.0000	328.15	1.4632
0.0458	328.15	1.4589
0.0955	328.15	1.4545
0.1560	328.15	1.4491
0.2040	328.15	1.4448
0.2515	328.15	1.4405
0.3012	328.15	1.4359
0.3491	328.15	1.4314
0.4060	328.15	1.4261
0.4530	328.15	1.4215
0.5010	328.15	1.4168
0.5520	328.15	1.412
0.6056	328.15	1.4071
0.6582	328.15	1.4023
0.7032	328.15	1.3981
0.7536	328.15	1.3937
0.8064	328.15	1.3889
0.8570	328.15	1.384
0.8967	328.15	1.38
0.9567	328.15	1.3747
1.0000	328.15	1.3718
0.0000	333.15	1.4617
0.0458	333.15	1.4574
0.0955	333.15	1.4529
0.1560	333.15	1.4471
0.2040	333.15	1.4428
0.2515	333.15	1.4387
0.3012	333.15	1.4343
0.3491	333.15	1.4299
0.4060	333.15	1.4248
0.4530	333.15	1.4204
0.5010	333.15	1.4161
0.5520	333.15	1.4113
0.6056	333.15	1.4062
0.6582	333.15	1.4013
0.7032	333.15	1.397
0.7536	333.15	1.3922
0.8064	333.15	1.3873
0.8570	333.15	1.383
0.8967	333.15	1.3797
0.9567	333.15	1.3743
1.0000	333.15	1.3697

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 95.99 (Liquid)

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
0.0000	303.15	1.4719
0.0458	303.15	1.4678
0.0955	303.15	1.4634
0.1560	303.15	1.458
0.2040	303.15	1.4538
0.2515	303.15	1.4496
0.3012	303.15	1.4451
0.3491	303.15	1.4409
0.4060	303.15	1.4359
0.4530	303.15	1.4317
0.5010	303.15	1.4275
0.5520	303.15	1.4229
0.6056	303.15	1.4182
0.6582	303.15	1.4135
0.7032	303.15	1.4095
0.7536	303.15	1.4051
0.8064	303.15	1.4004
0.8570	303.15	1.3959
0.8967	303.15	1.3924
0.9567	303.15	1.3863
1.0000	303.15	1.3822
0.0000	308.15	1.4694
0.0458	308.15	1.4653
0.0955	308.15	1.4609
0.1560	308.15	1.4554
0.2040	308.15	1.4511
0.2515	308.15	1.4469
0.3012	308.15	1.4424
0.3491	308.15	1.4382
0.4060	308.15	1.4331
0.4530	308.15	1.4288
0.5010	308.15	1.4245
0.5520	308.15	1.42
0.6056	308.15	1.4152
0.6582	308.15	1.4105
0.7032	308.15	1.4064
0.7536	308.15	1.4019
0.8064	308.15	1.3972
0.8570	308.15	1.3927
0.8967	308.15	1.389
0.9567	308.15	1.3838
1.0000	308.15	1.3803
0.0000	313.15	1.4673
0.0458	313.15	1.4631
0.0955	313.15	1.4587
0.1560	313.15	1.4532
0.2040	313.15	1.4489
0.2515	313.15	1.4446
0.3012	313.15	1.4402
0.3491	313.15	1.4359
0.4060	313.15	1.4308
0.4530	313.15	1.4265
0.5010	313.15	1.4222
0.5520	313.15	1.4176
0.6056	313.15	1.4128
0.6582	313.15	1.4081
0.7032	313.15	1.404
0.7536	313.15	1.3995
0.8064	313.15	1.3947
0.8570	313.15	1.3902
0.8967	313.15	1.3866
0.9567	313.15	1.3812
1.0000	313.15	1.3778
0.0000	318.15	1.4657
0.0458	318.15	1.4616
0.0955	318.15	1.457
0.1560	318.15	1.4515
0.2040	318.15	1.4472
0.2515	318.15	1.4429
0.3012	318.15	1.4384
0.3491	318.15	1.434
0.4060	318.15	1.4288
0.4530	318.15	1.4245
0.5010	318.15	1.4202
0.5520	318.15	1.4156
0.6056	318.15	1.4107
0.6582	318.15	1.4059
0.7032	318.15	1.4018
0.7536	318.15	1.3972
0.8064	318.15	1.3924
0.8570	318.15	1.3878
0.8967	318.15	1.3842
0.9567	318.15	1.3788
1.0000	318.15	1.3757
0.0000	323.15	1.4645
0.0458	323.15	1.4603
0.0955	323.15	1.4557
0.1560	323.15	1.4501
0.2040	323.15	1.4457
0.2515	323.15	1.4413
0.3012	323.15	1.4367
0.3491	323.15	1.4323
0.4060	323.15	1.427
0.4530	323.15	1.4227
0.5010	323.15	1.4183
0.5520	323.15	1.4136
0.6056	323.15	1.4087
0.6582	323.15	1.4038
0.7032	323.15	1.3997
0.7536	323.15	1.395
0.8064	323.15	1.3901
0.8570	323.15	1.3855
0.8967	323.15	1.3818
0.9567	323.15	1.3763
1.0000	323.15	1.3737
0.0000	328.15	1.4632
0.0458	328.15	1.4589
0.0955	328.15	1.4545
0.1560	328.15	1.4491
0.2040	328.15	1.4448
0.2515	328.15	1.4405
0.3012	328.15	1.4359
0.3491	328.15	1.4314
0.4060	328.15	1.4261
0.4530	328.15	1.4215
0.5010	328.15	1.4168
0.5520	328.15	1.412
0.6056	328.15	1.4071
0.6582	328.15	1.4023
0.7032	328.15	1.3981
0.7536	328.15	1.3937
0.8064	328.15	1.3889
0.8570	328.15	1.384
0.8967	328.15	1.38
0.9567	328.15	1.3747
1.0000	328.15	1.3718
0.0000	333.15	1.4617
0.0458	333.15	1.4574
0.0955	333.15	1.4529
0.1560	333.15	1.4471
0.2040	333.15	1.4428
0.2515	333.15	1.4387
0.3012	333.15	1.4343
0.3491	333.15	1.4299
0.4060	333.15	1.4248
0.4530	333.15	1.4204
0.5010	333.15	1.4161
0.5520	333.15	1.4113
0.6056	333.15	1.4062
0.6582	333.15	1.4013
0.7032	333.15	1.397
0.7536	333.15	1.3922
0.8064	333.15	1.3873
0.8570	333.15	1.383
0.8967	333.15	1.3797
0.9567	333.15	1.3743
1.0000	333.15	1.3697

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 95.99 (Liquid)

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	303.15	1253.99
0.0458	303.15	1231.81
0.0955	303.15	1208.28
0.1560	303.15	1179.3
0.2040	303.15	1156.31
0.2515	303.15	1133.55
0.3012	303.15	1109.73
0.3491	303.15	1086.79
0.4060	303.15	1059.55
0.4530	303.15	1037.02
0.5010	303.15	1014.02
0.5520	303.15	989.58
0.6056	303.15	963.92
0.6582	303.15	938.72
0.7032	303.15	917.16
0.7536	303.15	893.03
0.8064	303.15	867.71
0.8570	303.15	843.49
0.8967	303.15	824.44
0.9567	303.15	795.51
1.0000	303.15	775.47
0.0000	308.15	1250.84
0.0458	308.15	1228.56
0.0955	308.15	1204.91
0.1560	308.15	1175.79
0.2040	308.15	1152.68
0.2515	308.15	1129.81
0.3012	308.15	1105.87
0.3491	308.15	1082.81
0.4060	308.15	1055.43
0.4530	308.15	1032.8
0.5010	308.15	1009.67
0.5520	308.15	985.12
0.6056	308.15	959.33
0.6582	308.15	933.99
0.7032	308.15	912.33
0.7536	308.15	888.07
0.8064	308.15	862.63
0.8570	308.15	838.29
0.8967	308.15	819.14
0.9567	308.15	790.27
1.0000	308.15	770.21
0.0000	313.15	1247.69
0.0458	313.15	1225.31
0.0955	313.15	1201.55
0.1560	313.15	1172.28
0.2040	313.15	1149.05
0.2515	313.15	1126.07
0.3012	313.15	1102.01
0.3491	313.15	1078.83
0.4060	313.15	1051.32
0.4530	313.15	1028.57
0.5010	313.15	1005.33
0.5520	313.15	980.65
0.6056	313.15	954.73
0.6582	313.15	929.27
0.7032	313.15	907.5
0.7536	313.15	883.12
0.8064	313.15	857.55
0.8570	313.15	833.08
0.8967	313.15	813.84
0.9567	313.15	784.89
1.0000	313.15	764.86
0.0000	318.15	1244.54
0.0458	318.15	1222.06
0.0955	318.15	1198.18
0.1560	318.15	1168.77
0.2040	318.15	1145.42
0.2515	318.15	1122.33
0.3012	318.15	1098.15
0.3491	318.15	1074.86
0.4060	318.15	1047.2
0.4530	318.15	1024.34
0.5010	318.15	1000.99
0.5520	318.15	976.18
0.6056	318.15	950.13
0.6582	318.15	924.55
0.7032	318.15	902.66
0.7536	318.15	878.17
0.8064	318.15	852.47
0.8570	318.15	827.88
0.8967	318.15	808.54
0.9567	318.15	779.45
1.0000	318.15	759.44
0.0000	323.15	1241.39
0.0458	323.15	1218.81
0.0955	323.15	1194.82
0.1560	323.15	1165.25
0.2040	323.15	1141.79
0.2515	323.15	1118.58
0.3012	323.15	1094.28
0.3491	323.15	1070.88
0.4060	323.15	1043.09
0.4530	323.15	1020.11
0.5010	323.15	996.64
0.5520	323.15	971.71
0.6056	323.15	945.54
0.6582	323.15	919.82
0.7032	323.15	897.83
0.7536	323.15	873.21
0.8064	323.15	847.39
0.8570	323.15	822.68
0.8967	323.15	803.25
0.9567	323.15	773.94
1.0000	323.15	753.94
0.0000	328.15	1238.24
0.0458	328.15	1215.56
0.0955	328.15	1191.45
0.1560	328.15	1161.74
0.2040	328.15	1138.17
0.2515	328.15	1114.84
0.3012	328.15	1090.42
0.3491	328.15	1066.9
0.4060	328.15	1038.97
0.4530	328.15	1015.88
0.5010	328.15	992.3
0.5520	328.15	967.25
0.6056	328.15	940.94
0.6582	328.15	915.1
0.7032	328.15	893.0
0.7536	328.15	868.26
0.8064	328.15	842.31
0.8570	328.15	817.47
0.8967	328.15	797.95
0.9567	328.15	768.5
1.0000	328.15	748.36
0.0000	333.15	1235.09
0.0458	333.15	1212.31
0.0955	333.15	1188.09
0.1560	333.15	1158.23
0.2040	333.15	1134.54
0.2515	333.15	1111.1
0.3012	333.15	1086.56
0.3491	333.15	1062.92
0.4060	333.15	1034.86
0.4530	333.15	1011.65
0.5010	333.15	987.95
0.5520	333.15	962.78
0.6056	333.15	936.34
0.6582	333.15	910.38
0.7032	333.15	888.17
0.7536	333.15	863.31
0.8064	333.15	837.23
0.8570	333.15	812.27
0.8967	333.15	792.65
0.9567	333.15	763.05
1.0000	333.15	742.7

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 95.99 (Liquid)

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
0.0000	303.15	1253.99
0.0458	303.15	1231.81
0.0955	303.15	1208.28
0.1560	303.15	1179.3
0.2040	303.15	1156.31
0.2515	303.15	1133.55
0.3012	303.15	1109.73
0.3491	303.15	1086.79
0.4060	303.15	1059.55
0.4530	303.15	1037.02
0.5010	303.15	1014.02
0.5520	303.15	989.58
0.6056	303.15	963.92
0.6582	303.15	938.72
0.7032	303.15	917.16
0.7536	303.15	893.03
0.8064	303.15	867.71
0.8570	303.15	843.49
0.8967	303.15	824.44
0.9567	303.15	795.51
1.0000	303.15	775.47
0.0000	308.15	1250.84
0.0458	308.15	1228.56
0.0955	308.15	1204.91
0.1560	308.15	1175.79
0.2040	308.15	1152.68
0.2515	308.15	1129.81
0.3012	308.15	1105.87
0.3491	308.15	1082.81
0.4060	308.15	1055.43
0.4530	308.15	1032.8
0.5010	308.15	1009.67
0.5520	308.15	985.12
0.6056	308.15	959.33
0.6582	308.15	933.99
0.7032	308.15	912.33
0.7536	308.15	888.07
0.8064	308.15	862.63
0.8570	308.15	838.29
0.8967	308.15	819.14
0.9567	308.15	790.27
1.0000	308.15	770.21
0.0000	313.15	1247.69
0.0458	313.15	1225.31
0.0955	313.15	1201.55
0.1560	313.15	1172.28
0.2040	313.15	1149.05
0.2515	313.15	1126.07
0.3012	313.15	1102.01
0.3491	313.15	1078.83
0.4060	313.15	1051.32
0.4530	313.15	1028.57
0.5010	313.15	1005.33
0.5520	313.15	980.65
0.6056	313.15	954.73
0.6582	313.15	929.27
0.7032	313.15	907.5
0.7536	313.15	883.12
0.8064	313.15	857.55
0.8570	313.15	833.08
0.8967	313.15	813.84
0.9567	313.15	784.89
1.0000	313.15	764.86
0.0000	318.15	1244.54
0.0458	318.15	1222.06
0.0955	318.15	1198.18
0.1560	318.15	1168.77
0.2040	318.15	1145.42
0.2515	318.15	1122.33
0.3012	318.15	1098.15
0.3491	318.15	1074.86
0.4060	318.15	1047.2
0.4530	318.15	1024.34
0.5010	318.15	1000.99
0.5520	318.15	976.18
0.6056	318.15	950.13
0.6582	318.15	924.55
0.7032	318.15	902.66
0.7536	318.15	878.17
0.8064	318.15	852.47
0.8570	318.15	827.88
0.8967	318.15	808.54
0.9567	318.15	779.45
1.0000	318.15	759.44
0.0000	323.15	1241.39
0.0458	323.15	1218.81
0.0955	323.15	1194.82
0.1560	323.15	1165.25
0.2040	323.15	1141.79
0.2515	323.15	1118.58
0.3012	323.15	1094.28
0.3491	323.15	1070.88
0.4060	323.15	1043.09
0.4530	323.15	1020.11
0.5010	323.15	996.64
0.5520	323.15	971.71
0.6056	323.15	945.54
0.6582	323.15	919.82
0.7032	323.15	897.83
0.7536	323.15	873.21
0.8064	323.15	847.39
0.8570	323.15	822.68
0.8967	323.15	803.25
0.9567	323.15	773.94
1.0000	323.15	753.94
0.0000	328.15	1238.24
0.0458	328.15	1215.56
0.0955	328.15	1191.45
0.1560	328.15	1161.74
0.2040	328.15	1138.17
0.2515	328.15	1114.84
0.3012	328.15	1090.42
0.3491	328.15	1066.9
0.4060	328.15	1038.97
0.4530	328.15	1015.88
0.5010	328.15	992.3
0.5520	328.15	967.25
0.6056	328.15	940.94
0.6582	328.15	915.1
0.7032	328.15	893.0
0.7536	328.15	868.26
0.8064	328.15	842.31
0.8570	328.15	817.47
0.8967	328.15	797.95
0.9567	328.15	768.5
1.0000	328.15	748.36
0.0000	333.15	1235.09
0.0458	333.15	1212.31
0.0955	333.15	1188.09
0.1560	333.15	1158.23
0.2040	333.15	1134.54
0.2515	333.15	1111.1
0.3012	333.15	1086.56
0.3491	333.15	1062.92
0.4060	333.15	1034.86
0.4530	333.15	1011.65
0.5010	333.15	987.95
0.5520	333.15	962.78
0.6056	333.15	936.34
0.6582	333.15	910.38
0.7032	333.15	888.17
0.7536	333.15	863.31
0.8064	333.15	837.23
0.8570	333.15	812.27
0.8967	333.15	792.65
0.9567	333.15	763.05
1.0000	333.15	742.7

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Pressure, kPa - Gas	Boiling temperature at pressure P, K - Gas
0.0000	66.66	547.25
0.0146	66.66	511.98
0.0255	66.66	490.85
0.0302	66.66	483.68
0.0491	66.66	460.78
0.0996	66.66	427.89
0.1523	66.66	409.91
0.2009	66.66	399.12
0.3035	66.66	383.64
0.4024	66.66	373.56
0.5041	66.66	365.79
0.6033	66.66	359.79
0.7019	66.66	354.91
0.8026	66.66	350.80
0.8645	66.66	348.65
0.9022	66.66	347.47
0.9490	66.66	346.13
0.9646	66.66	345.72
0.9746	66.66	345.46
0.9852	66.66	345.19
1.0000	66.66	344.84
0.0000	79.99	553.96
0.0146	79.99	520.26
0.0255	79.99	500.05
0.0302	79.99	492.22
0.0491	79.99	469.36
0.0996	79.99	436.04
0.1523	79.99	417.08
0.2009	79.99	405.58
0.3035	79.99	389.42
0.4024	79.99	378.96
0.5041	79.99	370.91
0.6033	79.99	364.70
0.7019	79.99	359.65
0.8026	79.99	355.40
0.8645	79.99	353.18
0.9022	79.99	351.96
0.9490	79.99	350.58
0.9646	79.99	350.15
0.9746	79.99	349.88
0.9852	79.99	349.61
1.0000	79.99	349.23
0.0000	95.99	560.95
0.0146	95.99	528.86
0.0255	95.99	509.15
0.0302	95.99	501.65
0.0491	95.99	478.85
0.0996	95.99	443.55
0.1523	95.99	423.95
0.2009	95.99	412.20
0.3035	95.99	395.40
0.4024	95.99	384.54
0.5041	95.99	376.19
0.6033	95.99	369.78
0.7019	95.99	364.57
0.8026	95.99	360.18
0.8645	95.99	357.88
0.9022	95.99	356.62
0.9490	95.99	355.19
0.9646	95.99	354.74
0.9746	95.99	354.47
0.9852	95.99	354.18
1.0000	95.99	353.80

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Pressure, kPa - Gas	Boiling temperature at pressure P, K - Gas
0.0000	66.66	547.25
0.0146	66.66	511.98
0.0255	66.66	490.85
0.0302	66.66	483.68
0.0491	66.66	460.78
0.0996	66.66	427.89
0.1523	66.66	409.91
0.2009	66.66	399.12
0.3035	66.66	383.64
0.4024	66.66	373.56
0.5041	66.66	365.79
0.6033	66.66	359.79
0.7019	66.66	354.91
0.8026	66.66	350.80
0.8645	66.66	348.65
0.9022	66.66	347.47
0.9490	66.66	346.13
0.9646	66.66	345.72
0.9746	66.66	345.46
0.9852	66.66	345.19
1.0000	66.66	344.84
0.0000	79.99	553.96
0.0146	79.99	520.26
0.0255	79.99	500.05
0.0302	79.99	492.22
0.0491	79.99	469.36
0.0996	79.99	436.04
0.1523	79.99	417.08
0.2009	79.99	405.58
0.3035	79.99	389.42
0.4024	79.99	378.96
0.5041	79.99	370.91
0.6033	79.99	364.70
0.7019	79.99	359.65
0.8026	79.99	355.40
0.8645	79.99	353.18
0.9022	79.99	351.96
0.9490	79.99	350.58
0.9646	79.99	350.15
0.9746	79.99	349.88
0.9852	79.99	349.61
1.0000	79.99	349.23
0.0000	95.99	560.95
0.0146	95.99	528.86
0.0255	95.99	509.15
0.0302	95.99	501.65
0.0491	95.99	478.85
0.0996	95.99	443.55
0.1523	95.99	423.95
0.2009	95.99	412.20
0.3035	95.99	395.40
0.4024	95.99	384.54
0.5041	95.99	376.19
0.6033	95.99	369.78
0.7019	95.99	364.57
0.8026	95.99	360.18
0.8645	95.99	357.88
0.9022	95.99	356.62
0.9490	95.99	355.19
0.9646	95.99	354.74
0.9746	95.99	354.47
0.9852	95.99	354.18
1.0000	95.99	353.80

Sources

• Experimental and modeling vapor-liquid equilibrium for the binary systems {ethanol(1) + glycerol(2)} and {tert-butanol(1) + glycerol(2)} at high pressures
• Isobaric Phase Equilibrium of tert-Butyl Alcohol + Glycerol at Local and Subatmospheric Pressures, Volumetric Properties, and Molar Refractivity from 303.15 to 333.15 K of tert-Butyl Alcohol + Glycerol, tert-Butyl Alcohol + Water, and Water + Glycerol Binary Systems