Mixture of 1-Butanol + Pentane, 2,2,4-trimethyl-

Datasets

1. Mole fraction (6)
2. η - Viscosity, Pa*s (2)
3. Excess molar enthalpy (molar enthalpy (6)
4. P_vap - Vapor or sublimation pressure, kPa (6)
5. n₀ - Refractive index (Na D-line) (4)
6. ρ_l - Mass density, kg/m3 (6)
7. c_sound,fluid - Speed of Sound, m/s (4)
8. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Gas
0.0000	0.0000
0.0050	0.0385
0.0212	0.1320
0.0330	0.1863
0.0425	0.2334
0.0525	0.2848
0.0805	0.3863
0.0873	0.4107
0.1202	0.4597
0.1768	0.5457
0.2518	0.6079
0.3803	0.6671
0.5028	0.7031
0.6521	0.7410
0.7542	0.7592
0.7819	0.7713
0.7828	0.7669
0.8351	0.7856
0.8749	0.8035
0.8914	0.8153
0.9032	0.8265
0.9209	0.8414
0.9406	0.8646
0.9639	0.8991
0.9827	0.9455
1.0000	1.0000

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
308.15	0.0370	0.0580
308.15	0.0690	0.0710
308.15	0.0970	0.0780
308.15	0.1500	0.0880
308.15	0.1720	0.0890
308.15	0.2340	0.1000
308.15	0.3130	0.1120
308.15	0.4200	0.1290
308.15	0.4790	0.1340
308.15	0.5100	0.1380
308.15	0.5530	0.1420
308.15	0.5970	0.1500
308.15	0.6180	0.1510
308.15	0.6690	0.1590
308.15	0.7050	0.1670
308.15	0.7370	0.1770
308.15	0.8010	0.1960
308.15	0.8350	0.2180
308.15	0.8630	0.2440
308.15	0.8910	0.2780
308.15	0.9460	0.4060
308.15	0.9720	0.5600
308.15	0.9940	0.8460
313.15	0.0370	0.0640
313.15	0.0690	0.0810
313.15	0.0970	0.0880
313.15	0.1500	0.0970
313.15	0.1720	0.1010
313.15	0.2290	0.1070
313.15	0.2390	0.1080
313.15	0.2490	0.1090
313.15	0.3110	0.1180
313.15	0.3150	0.1180
313.15	0.4200	0.1380
313.15	0.4790	0.1480
313.15	0.5310	0.1560
313.15	0.5970	0.1630
313.15	0.6180	0.1650
313.15	0.6690	0.1780
313.15	0.7050	0.1870
313.15	0.7370	0.1980
313.15	0.7660	0.2090
313.15	0.8180	0.2320
313.15	0.8630	0.2730
313.15	0.9430	0.4290
313.15	0.9940	0.8650
318.15	0.0370	0.0710
318.15	0.0830	0.0930
318.15	0.1610	0.1090
318.15	0.2390	0.1190
318.15	0.3130	0.1300
318.15	0.4200	0.1470
318.15	0.4790	0.1670
318.15	0.5100	0.1680
318.15	0.5530	0.1750
318.15	0.5970	0.1810
318.15	0.6180	0.1850
318.15	0.6870	0.2000
318.15	0.7370	0.2190
318.15	0.7830	0.2360
318.15	0.8490	0.2840
318.15	0.9110	0.3700
318.15	0.9430	0.4640
318.15	0.9660	0.5780
318.15	0.9940	0.8800

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0797	0.0991
0.1015	0.0960
0.1020	0.1012
0.1066	0.1013
0.3039	0.1572
0.3633	0.1671
0.3638	0.1691
0.3837	0.1700
0.4933	0.1768
0.5897	0.1888
0.6242	0.1905
0.6624	0.2011
0.6657	0.2033
0.7458	0.2220
0.8359	0.2470
0.8623	0.2524
0.8831	0.2574
0.9191	0.2834
0.9230	0.2936
0.9483	0.3532
0.9751	0.4642

Mole fraction of Pentane, 2,2,4-trimethyl- (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Gas
0.0000	0.0000
0.0050	0.0385
0.0212	0.1320
0.0330	0.1863
0.0425	0.2334
0.0525	0.2848
0.0805	0.3863
0.0873	0.4107
0.1202	0.4597
0.1768	0.5457
0.2518	0.6079
0.3803	0.6671
0.5028	0.7031
0.6521	0.7410
0.7542	0.7592
0.7819	0.7713
0.7828	0.7669
0.8351	0.7856
0.8749	0.8035
0.8914	0.8153
0.9032	0.8265
0.9209	0.8414
0.9406	0.8646
0.9639	0.8991
0.9827	0.9455
1.0000	1.0000

Mole fraction of 1-Butanol (1) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
308.15	0.0370	0.0580
308.15	0.0690	0.0710
308.15	0.0970	0.0780
308.15	0.1500	0.0880
308.15	0.1720	0.0890
308.15	0.2340	0.1000
308.15	0.3130	0.1120
308.15	0.4200	0.1290
308.15	0.4790	0.1340
308.15	0.5100	0.1380
308.15	0.5530	0.1420
308.15	0.5970	0.1500
308.15	0.6180	0.1510
308.15	0.6690	0.1590
308.15	0.7050	0.1670
308.15	0.7370	0.1770
308.15	0.8010	0.1960
308.15	0.8350	0.2180
308.15	0.8630	0.2440
308.15	0.8910	0.2780
308.15	0.9460	0.4060
308.15	0.9720	0.5600
308.15	0.9940	0.8460
313.15	0.0370	0.0640
313.15	0.0690	0.0810
313.15	0.0970	0.0880
313.15	0.1500	0.0970
313.15	0.1720	0.1010
313.15	0.2290	0.1070
313.15	0.2390	0.1080
313.15	0.2490	0.1090
313.15	0.3110	0.1180
313.15	0.3150	0.1180
313.15	0.4200	0.1380
313.15	0.4790	0.1480
313.15	0.5310	0.1560
313.15	0.5970	0.1630
313.15	0.6180	0.1650
313.15	0.6690	0.1780
313.15	0.7050	0.1870
313.15	0.7370	0.1980
313.15	0.7660	0.2090
313.15	0.8180	0.2320
313.15	0.8630	0.2730
313.15	0.9430	0.4290
313.15	0.9940	0.8650
318.15	0.0370	0.0710
318.15	0.0830	0.0930
318.15	0.1610	0.1090
318.15	0.2390	0.1190
318.15	0.3130	0.1300
318.15	0.4200	0.1470
318.15	0.4790	0.1670
318.15	0.5100	0.1680
318.15	0.5530	0.1750
318.15	0.5970	0.1810
318.15	0.6180	0.1850
318.15	0.6870	0.2000
318.15	0.7370	0.2190
318.15	0.7830	0.2360
318.15	0.8490	0.2840
318.15	0.9110	0.3700
318.15	0.9430	0.4640
318.15	0.9660	0.5780
318.15	0.9940	0.8800

Mole fraction of 1-Butanol (1) [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mole fraction of 1-Butanol (1) - Gas
0.0797	0.0991
0.1015	0.0960
0.1020	0.1012
0.1066	0.1013
0.3039	0.1572
0.3633	0.1671
0.3638	0.1691
0.3837	0.1700
0.4933	0.1768
0.5897	0.1888
0.6242	0.1905
0.6624	0.2011
0.6657	0.2033
0.7458	0.2220
0.8359	0.2470
0.8623	0.2524
0.8831	0.2574
0.9191	0.2834
0.9230	0.2936
0.9483	0.3532
0.9751	0.4642

Viscosity, Pa*s [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	0.3002	100.00	0.0007
293.15	0.3002	1000.00	0.0007
293.15	0.3002	5000.00	0.0007
293.15	0.3002	10000.00	0.0007
293.15	0.3002	20000.00	0.0008
293.15	0.3002	30000.00	0.0009
293.15	0.3002	40000.00	0.0010
293.15	0.3002	50000.00	0.0011
293.15	0.3002	60000.00	0.0012
293.15	0.3002	70000.00	0.0013
293.15	0.3002	80000.00	0.0014
293.15	0.3002	100000.00	0.0017
293.15	0.3002	120000.00	0.0019
293.15	0.3002	140000.00	0.0022
313.15	0.3002	100.00	0.0005
313.15	0.3002	1000.00	0.0005
313.15	0.3002	5000.00	0.0005
313.15	0.3002	10000.00	0.0006
313.15	0.3002	20000.00	0.0006
313.15	0.3002	30000.00	0.0007
313.15	0.3002	40000.00	0.0008
313.15	0.3002	50000.00	0.0008
313.15	0.3002	60000.00	0.0009
313.15	0.3002	70000.00	0.0010
313.15	0.3002	80000.00	0.0011
313.15	0.3002	100000.00	0.0012
313.15	0.3002	120000.00	0.0014
313.15	0.3002	140000.00	0.0016
333.15	0.3002	100.00	0.0004
333.15	0.3002	1000.00	0.0004
333.15	0.3002	5000.00	0.0004
333.15	0.3002	10000.00	0.0004
333.15	0.3002	20000.00	0.0005
333.15	0.3002	30000.00	0.0006
333.15	0.3002	40000.00	0.0006
333.15	0.3002	50000.00	0.0007
333.15	0.3002	60000.00	0.0007
333.15	0.3002	70000.00	0.0008
333.15	0.3002	80000.00	0.0009
333.15	0.3002	100000.00	0.0010
333.15	0.3002	120000.00	0.0011
333.15	0.3002	140000.00	0.0013
353.15	0.3002	100.00	0.0003
353.15	0.3002	1000.00	0.0003
353.15	0.3002	5000.00	0.0003
353.15	0.3002	10000.00	0.0004
353.15	0.3002	20000.00	0.0004
353.15	0.3002	30000.00	0.0004
353.15	0.3002	40000.00	0.0005
353.15	0.3002	50000.00	0.0005
353.15	0.3002	60000.00	0.0006
353.15	0.3002	70000.00	0.0006
353.15	0.3002	80000.00	0.0007
353.15	0.3002	100000.00	0.0008
353.15	0.3002	120000.00	0.0009
353.15	0.3002	140000.00	0.0010
293.15	0.5003	100.00	0.0009
293.15	0.5003	1000.00	0.0009
293.15	0.5003	5000.00	0.0010
293.15	0.5003	10000.00	0.0010
293.15	0.5003	20000.00	0.0011
293.15	0.5003	30000.00	0.0013
293.15	0.5003	40000.00	0.0014
293.15	0.5003	50000.00	0.0016
293.15	0.5003	60000.00	0.0017
293.15	0.5003	70000.00	0.0019
293.15	0.5003	80000.00	0.0021
293.15	0.5003	100000.00	0.0024
293.15	0.5003	120000.00	0.0027
293.15	0.5003	140000.00	0.0031
313.15	0.5003	100.00	0.0006
313.15	0.5003	1000.00	0.0006
313.15	0.5003	5000.00	0.0007
313.15	0.5003	10000.00	0.0007
313.15	0.5003	20000.00	0.0008
313.15	0.5003	30000.00	0.0009
313.15	0.5003	40000.00	0.0010
313.15	0.5003	50000.00	0.0011
313.15	0.5003	60000.00	0.0012
313.15	0.5003	70000.00	0.0013
313.15	0.5003	80000.00	0.0014
313.15	0.5003	100000.00	0.0016
313.15	0.5003	120000.00	0.0019
313.15	0.5003	140000.00	0.0021
333.15	0.5003	100.00	0.0005
333.15	0.5003	1000.00	0.0005
333.15	0.5003	5000.00	0.0005
333.15	0.5003	10000.00	0.0005
333.15	0.5003	20000.00	0.0006
333.15	0.5003	30000.00	0.0006
333.15	0.5003	40000.00	0.0007
333.15	0.5003	50000.00	0.0008
333.15	0.5003	60000.00	0.0009
333.15	0.5003	70000.00	0.0009
333.15	0.5003	80000.00	0.0010
333.15	0.5003	100000.00	0.0012
333.15	0.5003	120000.00	0.0014
333.15	0.5003	140000.00	0.0016
353.15	0.5003	100.00	0.0004
353.15	0.5003	1000.00	0.0004
353.15	0.5003	5000.00	0.0004
353.15	0.5003	10000.00	0.0004
353.15	0.5003	20000.00	0.0005
353.15	0.5003	30000.00	0.0005
353.15	0.5003	40000.00	0.0006
353.15	0.5003	50000.00	0.0006
353.15	0.5003	60000.00	0.0007
353.15	0.5003	70000.00	0.0007
353.15	0.5003	80000.00	0.0008
353.15	0.5003	100000.00	0.0009
353.15	0.5003	120000.00	0.0010
353.15	0.5003	140000.00	0.0011
293.15	0.8000	100.00	0.0018
293.15	0.8000	1000.00	0.0018
293.15	0.8000	5000.00	0.0018
293.15	0.8000	10000.00	0.0019
293.15	0.8000	20000.00	0.0022
293.15	0.8000	30000.00	0.0024
293.15	0.8000	40000.00	0.0026
293.15	0.8000	50000.00	0.0028
293.15	0.8000	60000.00	0.0030
293.15	0.8000	70000.00	0.0033
293.15	0.8000	80000.00	0.0035
293.15	0.8000	100000.00	0.0041
293.15	0.8000	120000.00	0.0047
293.15	0.8000	140000.00	0.0053
313.15	0.8000	100.00	0.0012
313.15	0.8000	1000.00	0.0012
313.15	0.8000	5000.00	0.0012
313.15	0.8000	10000.00	0.0013
313.15	0.8000	20000.00	0.0014
313.15	0.8000	30000.00	0.0015
313.15	0.8000	40000.00	0.0017
313.15	0.8000	50000.00	0.0018
313.15	0.8000	60000.00	0.0020
313.15	0.8000	70000.00	0.0021
313.15	0.8000	80000.00	0.0023
313.15	0.8000	100000.00	0.0026
313.15	0.8000	120000.00	0.0030
313.15	0.8000	140000.00	0.0033
333.15	0.8000	100.00	0.0008
333.15	0.8000	1000.00	0.0008
333.15	0.8000	5000.00	0.0008
333.15	0.8000	10000.00	0.0009
333.15	0.8000	20000.00	0.0010
333.15	0.8000	30000.00	0.0010
333.15	0.8000	40000.00	0.0011
333.15	0.8000	50000.00	0.0012
333.15	0.8000	60000.00	0.0013
333.15	0.8000	70000.00	0.0014
333.15	0.8000	80000.00	0.0015
333.15	0.8000	100000.00	0.0017
333.15	0.8000	120000.00	0.0020
333.15	0.8000	140000.00	0.0022
353.15	0.8000	100.00	0.0006
353.15	0.8000	1000.00	0.0006
353.15	0.8000	5000.00	0.0006
353.15	0.8000	10000.00	0.0006
353.15	0.8000	20000.00	0.0007
353.15	0.8000	30000.00	0.0007
353.15	0.8000	40000.00	0.0008
353.15	0.8000	50000.00	0.0009
353.15	0.8000	60000.00	0.0009
353.15	0.8000	70000.00	0.0010
353.15	0.8000	80000.00	0.0011
353.15	0.8000	100000.00	0.0012
353.15	0.8000	120000.00	0.0014
353.15	0.8000	140000.00	0.0015
293.15	1.0000	100.00	0.0030
298.15	1.0000	100.00	0.0026
313.15	1.0000	100.00	0.0018
323.15	1.0000	100.00	0.0014
333.15	1.0000	100.00	0.0012
348.15	1.0000	100.00	0.0009
353.15	1.0000	100.00	0.0008
293.15	1.0000	1000.00	0.0030
298.15	1.0000	1000.00	0.0026
313.15	1.0000	1000.00	0.0018
323.15	1.0000	1000.00	0.0014
333.15	1.0000	1000.00	0.0012
348.15	1.0000	1000.00	0.0009
353.15	1.0000	1000.00	0.0008
293.15	1.0000	5000.00	0.0031
298.15	1.0000	5000.00	0.0027
313.15	1.0000	5000.00	0.0019
323.15	1.0000	5000.00	0.0015
333.15	1.0000	5000.00	0.0012
348.15	1.0000	5000.00	0.0009
353.15	1.0000	5000.00	0.0008
293.15	1.0000	10000.00	0.0032
298.15	1.0000	10000.00	0.0028
313.15	1.0000	10000.00	0.0020
323.15	1.0000	10000.00	0.0016
333.15	1.0000	10000.00	0.0013
348.15	1.0000	10000.00	0.0009
353.15	1.0000	10000.00	0.0009
293.15	1.0000	20000.00	0.0035
298.15	1.0000	20000.00	0.0031
313.15	1.0000	20000.00	0.0021
323.15	1.0000	20000.00	0.0017
333.15	1.0000	20000.00	0.0014
348.15	1.0000	20000.00	0.0010
353.15	1.0000	20000.00	0.0009
293.15	1.0000	30000.00	0.0038
298.15	1.0000	30000.00	0.0033
313.15	1.0000	30000.00	0.0023
323.15	1.0000	30000.00	0.0018
333.15	1.0000	30000.00	0.0015
348.15	1.0000	30000.00	0.0011
353.15	1.0000	30000.00	0.0010
293.15	1.0000	40000.00	0.0041
298.15	1.0000	40000.00	0.0036
313.15	1.0000	40000.00	0.0025
323.15	1.0000	40000.00	0.0020
333.15	1.0000	40000.00	0.0016
348.15	1.0000	40000.00	0.0012
353.15	1.0000	40000.00	0.0011
293.15	1.0000	50000.00	0.0044
298.15	1.0000	50000.00	0.0039
313.15	1.0000	50000.00	0.0026
323.15	1.0000	50000.00	0.0021
333.15	1.0000	50000.00	0.0017
348.15	1.0000	50000.00	0.0013
353.15	1.0000	50000.00	0.0012
293.15	1.0000	60000.00	0.0047
298.15	1.0000	60000.00	0.0042
313.15	1.0000	60000.00	0.0029
323.15	1.0000	60000.00	0.0023
333.15	1.0000	60000.00	0.0019
348.15	1.0000	60000.00	0.0014
353.15	1.0000	60000.00	0.0013
293.15	1.0000	70000.00	0.0051
298.15	1.0000	70000.00	0.0045
313.15	1.0000	70000.00	0.0031
323.15	1.0000	70000.00	0.0024
333.15	1.0000	70000.00	0.0020
348.15	1.0000	70000.00	0.0015
353.15	1.0000	70000.00	0.0014
293.15	1.0000	80000.00	0.0054
298.15	1.0000	80000.00	0.0048
313.15	1.0000	80000.00	0.0032
323.15	1.0000	80000.00	0.0026
333.15	1.0000	80000.00	0.0021
348.15	1.0000	80000.00	0.0016
353.15	1.0000	80000.00	0.0015
293.15	1.0000	100000.00	0.0062
298.15	1.0000	100000.00	0.0054
313.15	1.0000	100000.00	0.0037
323.15	1.0000	100000.00	0.0030
333.15	1.0000	100000.00	0.0024
348.15	1.0000	100000.00	0.0018
353.15	1.0000	100000.00	0.0017
293.15	1.0000	120000.00	0.0070
298.15	1.0000	120000.00	0.0061
313.15	1.0000	120000.00	0.0042
323.15	1.0000	120000.00	0.0033
333.15	1.0000	120000.00	0.0026
348.15	1.0000	120000.00	0.0020
353.15	1.0000	120000.00	0.0019
293.15	1.0000	140000.00	0.0078
298.15	1.0000	140000.00	0.0068
313.15	1.0000	140000.00	0.0046
323.15	1.0000	140000.00	0.0037
333.15	1.0000	140000.00	0.0029
348.15	1.0000	140000.00	0.0023
353.15	1.0000	140000.00	0.0020

Viscosity, Pa*s [ref]

Fixed			Measured
Temperature, K - Liquid	Mole fraction of 1-Butanol (1) - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	0.3002	100.00	0.0007
293.15	0.3002	1000.00	0.0007
293.15	0.3002	5000.00	0.0007
293.15	0.3002	10000.00	0.0007
293.15	0.3002	20000.00	0.0008
293.15	0.3002	30000.00	0.0009
293.15	0.3002	40000.00	0.0010
293.15	0.3002	50000.00	0.0011
293.15	0.3002	60000.00	0.0012
293.15	0.3002	70000.00	0.0013
293.15	0.3002	80000.00	0.0014
293.15	0.3002	100000.00	0.0017
293.15	0.3002	120000.00	0.0019
293.15	0.3002	140000.00	0.0022
313.15	0.3002	100.00	0.0005
313.15	0.3002	1000.00	0.0005
313.15	0.3002	5000.00	0.0005
313.15	0.3002	10000.00	0.0006
313.15	0.3002	20000.00	0.0006
313.15	0.3002	30000.00	0.0007
313.15	0.3002	40000.00	0.0008
313.15	0.3002	50000.00	0.0008
313.15	0.3002	60000.00	0.0009
313.15	0.3002	70000.00	0.0010
313.15	0.3002	80000.00	0.0011
313.15	0.3002	100000.00	0.0012
313.15	0.3002	120000.00	0.0014
313.15	0.3002	140000.00	0.0016
333.15	0.3002	100.00	0.0004
333.15	0.3002	1000.00	0.0004
333.15	0.3002	5000.00	0.0004
333.15	0.3002	10000.00	0.0004
333.15	0.3002	20000.00	0.0005
333.15	0.3002	30000.00	0.0006
333.15	0.3002	40000.00	0.0006
333.15	0.3002	50000.00	0.0007
333.15	0.3002	60000.00	0.0007
333.15	0.3002	70000.00	0.0008
333.15	0.3002	80000.00	0.0009
333.15	0.3002	100000.00	0.0010
333.15	0.3002	120000.00	0.0011
333.15	0.3002	140000.00	0.0013
353.15	0.3002	100.00	0.0003
353.15	0.3002	1000.00	0.0003
353.15	0.3002	5000.00	0.0003
353.15	0.3002	10000.00	0.0004
353.15	0.3002	20000.00	0.0004
353.15	0.3002	30000.00	0.0004
353.15	0.3002	40000.00	0.0005
353.15	0.3002	50000.00	0.0005
353.15	0.3002	60000.00	0.0006
353.15	0.3002	70000.00	0.0006
353.15	0.3002	80000.00	0.0007
353.15	0.3002	100000.00	0.0008
353.15	0.3002	120000.00	0.0009
353.15	0.3002	140000.00	0.0010
293.15	0.5003	100.00	0.0009
293.15	0.5003	1000.00	0.0009
293.15	0.5003	5000.00	0.0010
293.15	0.5003	10000.00	0.0010
293.15	0.5003	20000.00	0.0011
293.15	0.5003	30000.00	0.0013
293.15	0.5003	40000.00	0.0014
293.15	0.5003	50000.00	0.0016
293.15	0.5003	60000.00	0.0017
293.15	0.5003	70000.00	0.0019
293.15	0.5003	80000.00	0.0021
293.15	0.5003	100000.00	0.0024
293.15	0.5003	120000.00	0.0027
293.15	0.5003	140000.00	0.0031
313.15	0.5003	100.00	0.0006
313.15	0.5003	1000.00	0.0006
313.15	0.5003	5000.00	0.0007
313.15	0.5003	10000.00	0.0007
313.15	0.5003	20000.00	0.0008
313.15	0.5003	30000.00	0.0009
313.15	0.5003	40000.00	0.0010
313.15	0.5003	50000.00	0.0011
313.15	0.5003	60000.00	0.0012
313.15	0.5003	70000.00	0.0013
313.15	0.5003	80000.00	0.0014
313.15	0.5003	100000.00	0.0016
313.15	0.5003	120000.00	0.0019
313.15	0.5003	140000.00	0.0021
333.15	0.5003	100.00	0.0005
333.15	0.5003	1000.00	0.0005
333.15	0.5003	5000.00	0.0005
333.15	0.5003	10000.00	0.0005
333.15	0.5003	20000.00	0.0006
333.15	0.5003	30000.00	0.0006
333.15	0.5003	40000.00	0.0007
333.15	0.5003	50000.00	0.0008
333.15	0.5003	60000.00	0.0009
333.15	0.5003	70000.00	0.0009
333.15	0.5003	80000.00	0.0010
333.15	0.5003	100000.00	0.0012
333.15	0.5003	120000.00	0.0014
333.15	0.5003	140000.00	0.0016
353.15	0.5003	100.00	0.0004
353.15	0.5003	1000.00	0.0004
353.15	0.5003	5000.00	0.0004
353.15	0.5003	10000.00	0.0004
353.15	0.5003	20000.00	0.0005
353.15	0.5003	30000.00	0.0005
353.15	0.5003	40000.00	0.0006
353.15	0.5003	50000.00	0.0006
353.15	0.5003	60000.00	0.0007
353.15	0.5003	70000.00	0.0007
353.15	0.5003	80000.00	0.0008
353.15	0.5003	100000.00	0.0009
353.15	0.5003	120000.00	0.0010
353.15	0.5003	140000.00	0.0011
293.15	0.8000	100.00	0.0018
293.15	0.8000	1000.00	0.0018
293.15	0.8000	5000.00	0.0018
293.15	0.8000	10000.00	0.0019
293.15	0.8000	20000.00	0.0022
293.15	0.8000	30000.00	0.0024
293.15	0.8000	40000.00	0.0026
293.15	0.8000	50000.00	0.0028
293.15	0.8000	60000.00	0.0030
293.15	0.8000	70000.00	0.0033
293.15	0.8000	80000.00	0.0035
293.15	0.8000	100000.00	0.0041
293.15	0.8000	120000.00	0.0047
293.15	0.8000	140000.00	0.0053
313.15	0.8000	100.00	0.0012
313.15	0.8000	1000.00	0.0012
313.15	0.8000	5000.00	0.0012
313.15	0.8000	10000.00	0.0013
313.15	0.8000	20000.00	0.0014
313.15	0.8000	30000.00	0.0015
313.15	0.8000	40000.00	0.0017
313.15	0.8000	50000.00	0.0018
313.15	0.8000	60000.00	0.0020
313.15	0.8000	70000.00	0.0021
313.15	0.8000	80000.00	0.0023
313.15	0.8000	100000.00	0.0026
313.15	0.8000	120000.00	0.0030
313.15	0.8000	140000.00	0.0033
333.15	0.8000	100.00	0.0008
333.15	0.8000	1000.00	0.0008
333.15	0.8000	5000.00	0.0008
333.15	0.8000	10000.00	0.0009
333.15	0.8000	20000.00	0.0010
333.15	0.8000	30000.00	0.0010
333.15	0.8000	40000.00	0.0011
333.15	0.8000	50000.00	0.0012
333.15	0.8000	60000.00	0.0013
333.15	0.8000	70000.00	0.0014
333.15	0.8000	80000.00	0.0015
333.15	0.8000	100000.00	0.0017
333.15	0.8000	120000.00	0.0020
333.15	0.8000	140000.00	0.0022
353.15	0.8000	100.00	0.0006
353.15	0.8000	1000.00	0.0006
353.15	0.8000	5000.00	0.0006
353.15	0.8000	10000.00	0.0006
353.15	0.8000	20000.00	0.0007
353.15	0.8000	30000.00	0.0007
353.15	0.8000	40000.00	0.0008
353.15	0.8000	50000.00	0.0009
353.15	0.8000	60000.00	0.0009
353.15	0.8000	70000.00	0.0010
353.15	0.8000	80000.00	0.0011
353.15	0.8000	100000.00	0.0012
353.15	0.8000	120000.00	0.0014
353.15	0.8000	140000.00	0.0015
293.15	1.0000	100.00	0.0030
298.15	1.0000	100.00	0.0026
313.15	1.0000	100.00	0.0018
323.15	1.0000	100.00	0.0014
333.15	1.0000	100.00	0.0012
348.15	1.0000	100.00	0.0009
353.15	1.0000	100.00	0.0008
293.15	1.0000	1000.00	0.0030
298.15	1.0000	1000.00	0.0026
313.15	1.0000	1000.00	0.0018
323.15	1.0000	1000.00	0.0014
333.15	1.0000	1000.00	0.0012
348.15	1.0000	1000.00	0.0009
353.15	1.0000	1000.00	0.0008
293.15	1.0000	5000.00	0.0031
298.15	1.0000	5000.00	0.0027
313.15	1.0000	5000.00	0.0019
323.15	1.0000	5000.00	0.0015
333.15	1.0000	5000.00	0.0012
348.15	1.0000	5000.00	0.0009
353.15	1.0000	5000.00	0.0008
293.15	1.0000	10000.00	0.0032
298.15	1.0000	10000.00	0.0028
313.15	1.0000	10000.00	0.0020
323.15	1.0000	10000.00	0.0016
333.15	1.0000	10000.00	0.0013
348.15	1.0000	10000.00	0.0009
353.15	1.0000	10000.00	0.0009
293.15	1.0000	20000.00	0.0035
298.15	1.0000	20000.00	0.0031
313.15	1.0000	20000.00	0.0021
323.15	1.0000	20000.00	0.0017
333.15	1.0000	20000.00	0.0014
348.15	1.0000	20000.00	0.0010
353.15	1.0000	20000.00	0.0009
293.15	1.0000	30000.00	0.0038
298.15	1.0000	30000.00	0.0033
313.15	1.0000	30000.00	0.0023
323.15	1.0000	30000.00	0.0018
333.15	1.0000	30000.00	0.0015
348.15	1.0000	30000.00	0.0011
353.15	1.0000	30000.00	0.0010
293.15	1.0000	40000.00	0.0041
298.15	1.0000	40000.00	0.0036
313.15	1.0000	40000.00	0.0025
323.15	1.0000	40000.00	0.0020
333.15	1.0000	40000.00	0.0016
348.15	1.0000	40000.00	0.0012
353.15	1.0000	40000.00	0.0011
293.15	1.0000	50000.00	0.0044
298.15	1.0000	50000.00	0.0039
313.15	1.0000	50000.00	0.0026
323.15	1.0000	50000.00	0.0021
333.15	1.0000	50000.00	0.0017
348.15	1.0000	50000.00	0.0013
353.15	1.0000	50000.00	0.0012
293.15	1.0000	60000.00	0.0047
298.15	1.0000	60000.00	0.0042
313.15	1.0000	60000.00	0.0029
323.15	1.0000	60000.00	0.0023
333.15	1.0000	60000.00	0.0019
348.15	1.0000	60000.00	0.0014
353.15	1.0000	60000.00	0.0013
293.15	1.0000	70000.00	0.0051
298.15	1.0000	70000.00	0.0045
313.15	1.0000	70000.00	0.0031
323.15	1.0000	70000.00	0.0024
333.15	1.0000	70000.00	0.0020
348.15	1.0000	70000.00	0.0015
353.15	1.0000	70000.00	0.0014
293.15	1.0000	80000.00	0.0054
298.15	1.0000	80000.00	0.0048
313.15	1.0000	80000.00	0.0032
323.15	1.0000	80000.00	0.0026
333.15	1.0000	80000.00	0.0021
348.15	1.0000	80000.00	0.0016
353.15	1.0000	80000.00	0.0015
293.15	1.0000	100000.00	0.0062
298.15	1.0000	100000.00	0.0054
313.15	1.0000	100000.00	0.0037
323.15	1.0000	100000.00	0.0030
333.15	1.0000	100000.00	0.0024
348.15	1.0000	100000.00	0.0018
353.15	1.0000	100000.00	0.0017
293.15	1.0000	120000.00	0.0070
298.15	1.0000	120000.00	0.0061
313.15	1.0000	120000.00	0.0042
323.15	1.0000	120000.00	0.0033
333.15	1.0000	120000.00	0.0026
348.15	1.0000	120000.00	0.0020
353.15	1.0000	120000.00	0.0019
293.15	1.0000	140000.00	0.0078
298.15	1.0000	140000.00	0.0068
313.15	1.0000	140000.00	0.0046
323.15	1.0000	140000.00	0.0037
333.15	1.0000	140000.00	0.0029
348.15	1.0000	140000.00	0.0023
353.15	1.0000	140000.00	0.0020

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0502	0.0672
0.1001	0.1400
0.1504	0.2108
0.2002	0.2765
0.2504	0.3390
0.3000	0.3956
0.3502	0.4491
0.4000	0.4977
0.4498	0.5404
0.5006	0.5789
0.5500	0.6056
0.5997	0.6236
0.6497	0.6309
0.6998	0.6248
0.7498	0.6087
0.7995	0.5799
0.8501	0.5362
0.9000	0.4733
0.9506	0.3739

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 313.15 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0502	0.1049
0.1001	0.2036
0.1505	0.3013
0.2003	0.3928
0.2505	0.4803
0.3001	0.5599
0.3504	0.6347
0.4001	0.7006
0.4499	0.7567
0.5008	0.8024
0.5501	0.8372
0.5999	0.8594
0.6498	0.8669
0.7000	0.8618
0.7500	0.8410
0.7996	0.8058
0.8502	0.7501
0.9001	0.6672
0.9506	0.5226

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500	0.3964
0.1000	0.5023
0.1502	0.5697
0.2000	0.5874
0.2995	0.6228
0.4000	0.6287
0.5001	0.5938
0.6002	0.5157
0.7000	0.4052
0.8000	0.2871
0.8499	0.2226
0.9000	0.1502
0.9499	0.0788

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0502	0.0672
0.1001	0.1400
0.1504	0.2108
0.2002	0.2765
0.2504	0.3390
0.3000	0.3956
0.3502	0.4491
0.4000	0.4977
0.4498	0.5404
0.5006	0.5789
0.5500	0.6056
0.5997	0.6236
0.6497	0.6309
0.6998	0.6248
0.7498	0.6087
0.7995	0.5799
0.8501	0.5362
0.9000	0.4733
0.9506	0.3739

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 313.15 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0502	0.1049
0.1001	0.2036
0.1505	0.3013
0.2003	0.3928
0.2505	0.4803
0.3001	0.5599
0.3504	0.6347
0.4001	0.7006
0.4499	0.7567
0.5008	0.8024
0.5501	0.8372
0.5999	0.8594
0.6498	0.8669
0.7000	0.8618
0.7500	0.8410
0.7996	0.8058
0.8502	0.7501
0.9001	0.6672
0.9506	0.5226

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0500	0.3964
0.1000	0.5023
0.1502	0.5697
0.2000	0.5874
0.2995	0.6228
0.4000	0.6287
0.5001	0.5938
0.6002	0.5157
0.7000	0.4052
0.8000	0.2871
0.8499	0.2226
0.9000	0.1502
0.9499	0.0788

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.7005	11.55
0.3006	13.50

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0797	16.40
0.1015	16.40
0.1020	16.40
0.1066	16.33
0.3039	16.13
0.3633	16.00
0.3638	15.93
0.3837	15.87
0.4933	15.53
0.5897	15.27
0.6242	15.07
0.6624	14.93
0.6657	14.93
0.7458	14.40
0.8359	13.60
0.8623	13.00
0.8831	12.53
0.9191	11.40
0.9230	11.27
0.9483	9.33
0.9751	7.20

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	13.01
0.0509	13.66
0.0981	13.71
0.1495	13.66
0.1993	13.62
0.2497	13.52
0.2992	13.42
0.3499	13.30
0.4003	13.15
0.4007	13.17
0.4501	12.96
0.4510	13.02
0.5008	12.76
0.5012	12.83
0.5504	12.54
0.5524	12.58
0.6002	12.28
0.6339	12.04
0.6508	11.93
0.7005	11.47
0.7511	10.87
0.7999	10.11
0.8493	9.09
0.8969	7.74
0.9528	5.39
1.0000	2.55

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.7005	11.55
0.3006	13.50

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0797	16.40
0.1015	16.40
0.1020	16.40
0.1066	16.33
0.3039	16.13
0.3633	16.00
0.3638	15.93
0.3837	15.87
0.4933	15.53
0.5897	15.27
0.6242	15.07
0.6624	14.93
0.6657	14.93
0.7458	14.40
0.8359	13.60
0.8623	13.00
0.8831	12.53
0.9191	11.40
0.9230	11.27
0.9483	9.33
0.9751	7.20

Vapor or sublimation pressure, kPa [ref]

Operational condition: Temperature, K = 313.15 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	13.01
0.0509	13.66
0.0981	13.71
0.1495	13.66
0.1993	13.62
0.2497	13.52
0.2992	13.42
0.3499	13.30
0.4003	13.15
0.4007	13.17
0.4501	12.96
0.4510	13.02
0.5008	12.76
0.5012	12.83
0.5504	12.54
0.5524	12.58
0.6002	12.28
0.6339	12.04
0.6508	11.93
0.7005	11.47
0.7511	10.87
0.7999	10.11
0.8493	9.09
0.8969	7.74
0.9528	5.39
1.0000	2.55

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0501	1.389
0.1001	1.3891
0.1501	1.3893
0.2000	1.3895
0.3001	1.39
0.3999	1.3907
0.5000	1.3915
0.5999	1.3924
0.6999	1.3935
0.8000	1.3947
0.8500	1.3953
0.9000	1.3959
0.9500	1.3965

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3972
0.0518	1.3966
0.1022	1.396
0.1512	1.3954
0.2028	1.3948
0.2535	1.3943
0.3042	1.3937
0.3535	1.3932
0.4049	1.3927
0.4534	1.3922
0.5032	1.3917
0.5534	1.3913
0.6041	1.3909
0.6558	1.3905
0.7046	1.3902
0.7521	1.3899
0.8047	1.3896
0.8521	1.3893
0.9005	1.3891
0.9502	1.389
1.0000	1.389

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0501	1.389
0.1001	1.3891
0.1501	1.3893
0.2000	1.3895
0.3001	1.39
0.3999	1.3907
0.5000	1.3915
0.5999	1.3924
0.6999	1.3935
0.8000	1.3947
0.8500	1.3953
0.9000	1.3959
0.9500	1.3965

Refractive index (Na D-line) [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Refractive index (Na D-line) - Liquid
0.0000	1.3972
0.0518	1.3966
0.1022	1.396
0.1512	1.3954
0.2028	1.3948
0.2535	1.3943
0.3042	1.3937
0.3535	1.3932
0.4049	1.3927
0.4534	1.3922
0.5032	1.3917
0.5534	1.3913
0.6041	1.3909
0.6558	1.3905
0.7046	1.3902
0.7521	1.3899
0.8047	1.3896
0.8521	1.3893
0.9005	1.3891
0.9502	1.389
1.0000	1.389

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0501	690.95
0.1001	694.28
0.1501	697.81
0.2000	701.56
0.3001	709.77
0.3999	718.98
0.5000	729.4
0.5999	741.16
0.6999	754.51
0.8000	769.68
0.8500	778.03
0.9000	786.94
0.9500	796.46

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	805.78
0.0518	795.39
0.1022	785.94
0.1512	777.34
0.2028	768.9
0.2535	761.12
0.3042	753.81
0.3535	747.12
0.4049	740.56
0.4534	734.72
0.5032	729.09
0.5534	723.73
0.6041	718.63
0.6558	713.71
0.7046	709.35
0.7521	705.31
0.8047	701.05
0.8521	697.48
0.9005	694.03
0.9502	690.74
1.0000	687.79

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	1.0000	687.68
298.15	0.9810	688.66
298.15	0.9619	689.83
298.15	0.9422	691.1
298.15	0.9078	693.42
298.15	0.8683	696.2
298.15	0.8095	700.58
298.15	0.7420	706.01
298.15	0.6787	711.51
298.15	0.6067	718.27
298.15	0.5458	724.43
298.15	0.4553	734.44
298.15	0.3932	741.94
298.15	0.3176	751.87
298.15	0.2621	759.76
298.15	0.2049	768.51
298.15	0.1426	778.75
298.15	0.0756	790.82
298.15	0.0310	799.41
298.15	0.0000	805.74
308.15	1.0000	679.45
308.15	0.9810	680.37
308.15	0.9619	681.51
308.15	0.9422	682.76
308.15	0.9078	685.07
308.15	0.8683	687.84
308.15	0.8095	692.21
308.15	0.7420	697.65
308.15	0.6787	703.15
308.15	0.6067	709.93
308.15	0.5458	716.13
308.15	0.4553	726.18
308.15	0.3932	733.74
308.15	0.3176	743.75
308.15	0.2621	751.67
308.15	0.2049	760.53
308.15	0.1426	770.87
308.15	0.0756	783.03
308.15	0.0310	791.7
308.15	0.0000	798.07
318.15	1.0000	671.3
318.15	0.9810	672.16
318.15	0.9619	673.25
318.15	0.9422	674.47
318.15	0.9078	676.75
318.15	0.8683	679.5
318.15	0.8095	683.87
318.15	0.7420	689.3
318.15	0.6787	694.8
318.15	0.6067	701.6
318.15	0.5458	707.81
318.15	0.4553	717.92
318.15	0.3932	725.51
318.15	0.3176	735.6
318.15	0.2621	743.61
318.15	0.2049	752.52
318.15	0.1426	762.95
318.15	0.0756	775.22
318.15	0.0310	783.95
318.15	0.0000	790.38
328.15	1.0000	663.17
328.15	0.9810	663.97
328.15	0.9619	664.98
328.15	0.9422	666.16
328.15	0.9078	668.4
328.15	0.8683	671.13
328.15	0.8095	675.5
328.15	0.7420	680.9
328.15	0.6787	686.39
328.15	0.6067	693.2
328.15	0.5458	699.42
328.15	0.4553	709.56
328.15	0.3932	717.19
328.15	0.3176	727.34
328.15	0.2621	735.41
328.15	0.2049	744.39
328.15	0.1426	754.91
328.15	0.0756	767.29
328.15	0.0310	776.09
328.15	0.0000	782.58

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Butanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.0501	690.95
0.1001	694.28
0.1501	697.81
0.2000	701.56
0.3001	709.77
0.3999	718.98
0.5000	729.4
0.5999	741.16
0.6999	754.51
0.8000	769.68
0.8500	778.03
0.9000	786.94
0.9500	796.46

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	805.78
0.0518	795.39
0.1022	785.94
0.1512	777.34
0.2028	768.9
0.2535	761.12
0.3042	753.81
0.3535	747.12
0.4049	740.56
0.4534	734.72
0.5032	729.09
0.5534	723.73
0.6041	718.63
0.6558	713.71
0.7046	709.35
0.7521	705.31
0.8047	701.05
0.8521	697.48
0.9005	694.03
0.9502	690.74
1.0000	687.79

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	1.0000	687.68
298.15	0.9810	688.66
298.15	0.9619	689.83
298.15	0.9422	691.1
298.15	0.9078	693.42
298.15	0.8683	696.2
298.15	0.8095	700.58
298.15	0.7420	706.01
298.15	0.6787	711.51
298.15	0.6067	718.27
298.15	0.5458	724.43
298.15	0.4553	734.44
298.15	0.3932	741.94
298.15	0.3176	751.87
298.15	0.2621	759.76
298.15	0.2049	768.51
298.15	0.1426	778.75
298.15	0.0756	790.82
298.15	0.0310	799.41
298.15	0.0000	805.74
308.15	1.0000	679.45
308.15	0.9810	680.37
308.15	0.9619	681.51
308.15	0.9422	682.76
308.15	0.9078	685.07
308.15	0.8683	687.84
308.15	0.8095	692.21
308.15	0.7420	697.65
308.15	0.6787	703.15
308.15	0.6067	709.93
308.15	0.5458	716.13
308.15	0.4553	726.18
308.15	0.3932	733.74
308.15	0.3176	743.75
308.15	0.2621	751.67
308.15	0.2049	760.53
308.15	0.1426	770.87
308.15	0.0756	783.03
308.15	0.0310	791.7
308.15	0.0000	798.07
318.15	1.0000	671.3
318.15	0.9810	672.16
318.15	0.9619	673.25
318.15	0.9422	674.47
318.15	0.9078	676.75
318.15	0.8683	679.5
318.15	0.8095	683.87
318.15	0.7420	689.3
318.15	0.6787	694.8
318.15	0.6067	701.6
318.15	0.5458	707.81
318.15	0.4553	717.92
318.15	0.3932	725.51
318.15	0.3176	735.6
318.15	0.2621	743.61
318.15	0.2049	752.52
318.15	0.1426	762.95
318.15	0.0756	775.22
318.15	0.0310	783.95
318.15	0.0000	790.38
328.15	1.0000	663.17
328.15	0.9810	663.97
328.15	0.9619	664.98
328.15	0.9422	666.16
328.15	0.9078	668.4
328.15	0.8683	671.13
328.15	0.8095	675.5
328.15	0.7420	680.9
328.15	0.6787	686.39
328.15	0.6067	693.2
328.15	0.5458	699.42
328.15	0.4553	709.56
328.15	0.3932	717.19
328.15	0.3176	727.34
328.15	0.2621	735.41
328.15	0.2049	744.39
328.15	0.1426	754.91
328.15	0.0756	767.29
328.15	0.0310	776.09
328.15	0.0000	782.58

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Temperature, K = 298.15 (Liquid)
• Frequency, MHz = 3 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1240.08
0.0518	1223.4
0.1022	1208.27
0.1512	1194.3
0.2028	1181.46
0.2535	1169.42
0.3042	1157.88
0.3535	1148.58
0.4049	1139.14
0.4534	1130.8
0.5032	1123.41
0.5534	1116.56
0.6041	1110.26
0.6558	1104.47
0.7046	1099.63
0.7521	1095.4
0.8047	1091.07
0.8521	1087.91
0.9005	1085.06
0.9502	1082.82
1.0000	1082.77

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Speed of sound, m/s - Liquid
298.15	1.0000	1082.7
298.15	0.9810	1082.1
298.15	0.9619	1082.3
298.15	0.9422	1082.9
298.15	0.9078	1084.5
298.15	0.8683	1086.7
298.15	0.8095	1090.6
298.15	0.7420	1095.9
298.15	0.6787	1101.9
298.15	0.6067	1109.8
298.15	0.5458	1117.4
298.15	0.4553	1130.7
298.15	0.3932	1141.1
298.15	0.3176	1155.5
298.15	0.2621	1167.3
298.15	0.2049	1180.8
298.15	0.1426	1196.8
298.15	0.0756	1216.0
298.15	0.0310	1229.7
298.15	0.0000	1239.9
308.15	1.0000	1041.1
308.15	0.9810	1040.9
308.15	0.9619	1040.7
308.15	0.9422	1041.5
308.15	0.9078	1043.1
308.15	0.8683	1045.4
308.15	0.8095	1049.5
308.15	0.7420	1055.1
308.15	0.6787	1061.3
308.15	0.6067	1069.5
308.15	0.5458	1077.5
308.15	0.4553	1091.4
308.15	0.3932	1102.3
308.15	0.3176	1117.5
308.15	0.2621	1130.0
308.15	0.2049	1144.2
308.15	0.1426	1161.1
308.15	0.0756	1181.3
308.15	0.0310	1195.8
308.15	0.0000	1206.6
318.15	1.0000	1000.1
318.15	0.9810	1000.1
318.15	0.9619	1000.0
318.15	0.9422	1000.6
318.15	0.9078	1002.2
318.15	0.8683	1004.6
318.15	0.8095	1008.8
318.15	0.7420	1014.7
318.15	0.6787	1021.1
318.15	0.6067	1029.7
318.15	0.5458	1038.1
318.15	0.4553	1052.6
318.15	0.3932	1063.9
318.15	0.3176	1079.8
318.15	0.2621	1092.5
318.15	0.2049	1107.8
318.15	0.1426	1125.6
318.15	0.0756	1146.9
318.15	0.0310	1162.1
318.15	0.0000	1173.4
328.15	1.0000	959.4
328.15	0.9810	959.7
328.15	0.9619	959.7
328.15	0.9422	960.2
328.15	0.9078	961.8
328.15	0.8683	964.3
328.15	0.8095	968.8
328.15	0.7420	974.8
328.15	0.6787	981.6
328.15	0.6067	990.4
328.15	0.5458	999.2
328.15	0.4553	1014.1
328.15	0.3932	1025.9
328.15	0.3176	1042.5
328.15	0.2621	1056.1
328.15	0.2049	1071.7
328.15	0.1426	1090.3
328.15	0.0756	1112.6
328.15	0.0310	1128.6
328.15	0.0000	1140.4

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 101.3 (Liquid)
• Temperature, K = 298.15 (Liquid)
• Frequency, MHz = 3 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Speed of sound, m/s - Liquid
0.0000	1240.08
0.0518	1223.4
0.1022	1208.27
0.1512	1194.3
0.2028	1181.46
0.2535	1169.42
0.3042	1157.88
0.3535	1148.58
0.4049	1139.14
0.4534	1130.8
0.5032	1123.41
0.5534	1116.56
0.6041	1110.26
0.6558	1104.47
0.7046	1099.63
0.7521	1095.4
0.8047	1091.07
0.8521	1087.91
0.9005	1085.06
0.9502	1082.82
1.0000	1082.77

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Speed of sound, m/s - Liquid
298.15	1.0000	1082.7
298.15	0.9810	1082.1
298.15	0.9619	1082.3
298.15	0.9422	1082.9
298.15	0.9078	1084.5
298.15	0.8683	1086.7
298.15	0.8095	1090.6
298.15	0.7420	1095.9
298.15	0.6787	1101.9
298.15	0.6067	1109.8
298.15	0.5458	1117.4
298.15	0.4553	1130.7
298.15	0.3932	1141.1
298.15	0.3176	1155.5
298.15	0.2621	1167.3
298.15	0.2049	1180.8
298.15	0.1426	1196.8
298.15	0.0756	1216.0
298.15	0.0310	1229.7
298.15	0.0000	1239.9
308.15	1.0000	1041.1
308.15	0.9810	1040.9
308.15	0.9619	1040.7
308.15	0.9422	1041.5
308.15	0.9078	1043.1
308.15	0.8683	1045.4
308.15	0.8095	1049.5
308.15	0.7420	1055.1
308.15	0.6787	1061.3
308.15	0.6067	1069.5
308.15	0.5458	1077.5
308.15	0.4553	1091.4
308.15	0.3932	1102.3
308.15	0.3176	1117.5
308.15	0.2621	1130.0
308.15	0.2049	1144.2
308.15	0.1426	1161.1
308.15	0.0756	1181.3
308.15	0.0310	1195.8
308.15	0.0000	1206.6
318.15	1.0000	1000.1
318.15	0.9810	1000.1
318.15	0.9619	1000.0
318.15	0.9422	1000.6
318.15	0.9078	1002.2
318.15	0.8683	1004.6
318.15	0.8095	1008.8
318.15	0.7420	1014.7
318.15	0.6787	1021.1
318.15	0.6067	1029.7
318.15	0.5458	1038.1
318.15	0.4553	1052.6
318.15	0.3932	1063.9
318.15	0.3176	1079.8
318.15	0.2621	1092.5
318.15	0.2049	1107.8
318.15	0.1426	1125.6
318.15	0.0756	1146.9
318.15	0.0310	1162.1
318.15	0.0000	1173.4
328.15	1.0000	959.4
328.15	0.9810	959.7
328.15	0.9619	959.7
328.15	0.9422	960.2
328.15	0.9078	961.8
328.15	0.8683	964.3
328.15	0.8095	968.8
328.15	0.7420	974.8
328.15	0.6787	981.6
328.15	0.6067	990.4
328.15	0.5458	999.2
328.15	0.4553	1014.1
328.15	0.3932	1025.9
328.15	0.3176	1042.5
328.15	0.2621	1056.1
328.15	0.2049	1071.7
328.15	0.1426	1090.3
328.15	0.0756	1112.6
328.15	0.0310	1128.6
328.15	0.0000	1140.4

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	390.25
0.0050	388.96
0.0212	385.91
0.0330	385.17
0.0425	383.97
0.0525	382.10
0.0805	379.36
0.0873	378.82
0.1202	377.06
0.1768	374.15
0.2518	371.63
0.3803	369.35
0.5028	368.24
0.6521	367.51
0.7542	367.30
0.7819	367.46
0.7828	367.36
0.8351	367.45
0.8749	367.59
0.8914	367.69
0.9032	367.80
0.9209	368.04
0.9406	368.40
0.9639	369.21
0.9827	370.42
1.0000	372.16

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Pentane, 2,2,4-trimethyl- (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	390.25
0.0050	388.96
0.0212	385.91
0.0330	385.17
0.0425	383.97
0.0525	382.10
0.0805	379.36
0.0873	378.82
0.1202	377.06
0.1768	374.15
0.2518	371.63
0.3803	369.35
0.5028	368.24
0.6521	367.51
0.7542	367.30
0.7819	367.46
0.7828	367.36
0.8351	367.45
0.8749	367.59
0.8914	367.69
0.9032	367.80
0.9209	368.04
0.9406	368.40
0.9639	369.21
0.9827	370.42
1.0000	372.16

Sources

• Excess enthalpies of oxygenated compounds + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and 2,2,4-trimethylpentane at 298.15 K
• Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
• Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
• Isobaric vapor-liquid equilibrium, density and speed of sound of binary mixtures 2,2,4-trimethylpentane + 1-butanol or dibutyl ether (DBE) at 101.3 kPa
• Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K
• Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
• Viscosities of binary mixtures containing 1-butanol + 2,2,4-trimethylpentane or + 1,2,4-trimethylbenzene at high pressures for the thermophysical characterization of biofuels
• Vapor-Liquid Equilibrium of Binary Mixtures. 2. Ethanol + 2,2,4-Trimethylpentane, 1-Butanol + 2,2,4-Trimethylpentane, and Ethanol + o-Xylene
• Isothermal Vapor Liquid Equilibrium Data of Propan-1-ol + 2,2,4-Trimethylpentane and Butan-1-ol + 2,2,4-Trimethylpentane at 318.15 K
• Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K