Mixture of Tetrahydropyran + 1-Butanol

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Tetrahydropyran

Name
Tetrahydropyran
InChI
InChI=1S/C5H10O/c1-2-4-6-5-3-1/h1-5H2
InChI Key
DHXVGJBLRPWPCS-UHFFFAOYSA-N
Formula
C5H10O
SMILES
C1CCOCC1
Mol. Weight (g/mol)
86.13
CAS
142-68-7

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. ρl - Mass density, kg/m3 (2)
  4. csound,fluid - Speed of Sound, m/s (2)
  5. Tboil - Boiling temperature at pressure P, K (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0478 0.0033
283.15 0.0969 0.0029
283.15 0.1984 0.0023
283.15 0.2880 0.0019
283.15 0.3973 0.0016
283.15 0.5005 0.0014
283.15 0.6788 0.0012
283.15 0.7023 0.0012
283.15 0.8041 0.0011
283.15 0.9024 0.0011
298.15 0.0478 0.0023
298.15 0.0969 0.0021
298.15 0.1984 0.0017
298.15 0.2880 0.0014
298.15 0.3973 0.0012
298.15 0.5005 0.0011
298.15 0.6788 0.0009
298.15 0.7023 0.0009
298.15 0.8041 0.0009
298.15 0.9024 0.0008
313.15 0.0478 0.0016
313.15 0.0969 0.0015
313.15 0.1984 0.0013
313.15 0.2880 0.0011
313.15 0.3973 0.0009
313.15 0.5005 0.0008
313.15 0.6788 0.0007
313.15 0.7023 0.0007
313.15 0.8041 0.0007
313.15 0.9024 0.0007

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Viscosity, Pa*s - Liquid
283.15 0.0478 0.0033
283.15 0.0969 0.0029
283.15 0.1984 0.0023
283.15 0.2880 0.0019
283.15 0.3973 0.0016
283.15 0.5005 0.0014
283.15 0.6788 0.0012
283.15 0.7023 0.0012
283.15 0.8041 0.0011
283.15 0.9024 0.0011
298.15 0.0478 0.0023
298.15 0.0969 0.0021
298.15 0.1984 0.0017
298.15 0.2880 0.0014
298.15 0.3973 0.0012
298.15 0.5005 0.0011
298.15 0.6788 0.0009
298.15 0.7023 0.0009
298.15 0.8041 0.0009
298.15 0.9024 0.0008
313.15 0.0478 0.0016
313.15 0.0969 0.0015
313.15 0.1984 0.0013
313.15 0.2880 0.0011
313.15 0.3973 0.0009
313.15 0.5005 0.0008
313.15 0.6788 0.0007
313.15 0.7023 0.0007
313.15 0.8041 0.0007
313.15 0.9024 0.0007

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

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
283.15 0.0400 0.1180
283.15 0.0900 0.2400
283.15 0.1880 0.4520
283.15 0.2880 0.6270
283.15 0.3900 0.7610
283.15 0.4900 0.8330
283.15 0.5930 0.8520
283.15 0.6940 0.8020
283.15 0.7960 0.6640
283.15 0.9010 0.4030
283.15 0.9520 0.2210
298.15 0.0400 0.1250
298.15 0.0900 0.2570
298.15 0.1880 0.4920
298.15 0.2880 0.6910
298.15 0.3900 0.8410
298.15 0.4900 0.9200
298.15 0.5930 0.9310
298.15 0.6940 0.8650
298.15 0.7960 0.6980
298.15 0.9010 0.4120
298.15 0.9520 0.2220
313.15 0.0400 0.1190
313.15 0.0900 0.2580
313.15 0.1880 0.5170
313.15 0.2880 0.7360
313.15 0.3900 0.8990
313.15 0.4900 0.9810
313.15 0.5930 0.9890
313.15 0.6940 0.9120
313.15 0.7960 0.7160
313.15 0.9010 0.4080
313.15 0.9520 0.2160

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

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
283.15 0.0400 0.1180
283.15 0.0900 0.2400
283.15 0.1880 0.4520
283.15 0.2880 0.6270
283.15 0.3900 0.7610
283.15 0.4900 0.8330
283.15 0.5930 0.8520
283.15 0.6940 0.8020
283.15 0.7960 0.6640
283.15 0.9010 0.4030
283.15 0.9520 0.2210
298.15 0.0400 0.1250
298.15 0.0900 0.2570
298.15 0.1880 0.4920
298.15 0.2880 0.6910
298.15 0.3900 0.8410
298.15 0.4900 0.9200
298.15 0.5930 0.9310
298.15 0.6940 0.8650
298.15 0.7960 0.6980
298.15 0.9010 0.4120
298.15 0.9520 0.2220
313.15 0.0400 0.1190
313.15 0.0900 0.2580
313.15 0.1880 0.5170
313.15 0.2880 0.7360
313.15 0.3900 0.8990
313.15 0.4900 0.9810
313.15 0.5930 0.9890
313.15 0.6940 0.9120
313.15 0.7960 0.7160
313.15 0.9010 0.4080
313.15 0.9520 0.2160

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Mass density, kg/m3 - Liquid
283.15 0.1036 825.58
283.15 0.2049 833.85
283.15 0.3039 841.76
283.15 0.4059 849.75
283.15 0.4905 856.26
283.15 0.6081 865.2
283.15 0.7057 872.53
283.15 0.8027 879.78
283.15 0.8990 887.01
298.15 0.0508 809.82
298.15 0.1039 814.08
298.15 0.2056 822.12
298.15 0.3050 829.77
298.15 0.4060 837.37
298.15 0.4909 843.65
298.15 0.6079 852.23
298.15 0.7054 859.31
298.15 0.8047 866.47
298.15 0.9043 873.67
298.15 0.9580 877.6
313.15 0.1039 802.15
313.15 0.2027 809.43
313.15 0.3254 818.28
313.15 0.4063 824.0
313.15 0.4883 829.7
313.15 0.6215 838.8
313.15 0.7037 844.36
313.15 0.8037 851.1
313.15 0.8978 857.5

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Mass density, kg/m3 - Liquid
283.15 0.1036 825.58
283.15 0.2049 833.85
283.15 0.3039 841.76
283.15 0.4059 849.75
283.15 0.4905 856.26
283.15 0.6081 865.2
283.15 0.7057 872.53
283.15 0.8027 879.78
283.15 0.8990 887.01
298.15 0.0508 809.82
298.15 0.1039 814.08
298.15 0.2056 822.12
298.15 0.3050 829.77
298.15 0.4060 837.37
298.15 0.4909 843.65
298.15 0.6079 852.23
298.15 0.7054 859.31
298.15 0.8047 866.47
298.15 0.9043 873.67
298.15 0.9580 877.6
313.15 0.1039 802.15
313.15 0.2027 809.43
313.15 0.3254 818.28
313.15 0.4063 824.0
313.15 0.4883 829.7
313.15 0.6215 838.8
313.15 0.7037 844.36
313.15 0.8037 851.1
313.15 0.8978 857.5

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Speed of sound, m/s - Liquid
283.15 0.0448 1294.9
283.15 0.1051 1298.7
283.15 0.2010 1304.0
283.15 0.3026 1309.0
283.15 0.4115 1313.8
283.15 0.5038 1317.5
283.15 0.6065 1321.9
283.15 0.7044 1326.1
283.15 0.7888 1330.0
283.15 0.8925 1334.9
283.15 0.9533 1337.6
298.15 0.0471 1245.5
298.15 0.0972 1247.7
298.15 0.2026 1251.7
298.15 0.2903 1254.4
298.15 0.3266 1255.4
298.15 0.3987 1257.3
298.15 0.5146 1260.2
298.15 0.6077 1262.6
298.15 0.7128 1265.5
298.15 0.7996 1267.9
298.15 0.8595 1269.5
298.15 0.8915 1270.4
298.15 0.9350 1271.5
313.15 0.1081 1189.1
313.15 0.1937 1190.6
313.15 0.2954 1192.1
313.15 0.4021 1193.4
313.15 0.5032 1194.4
313.15 0.6035 1195.1
313.15 0.6615 1195.5
313.15 0.7114 1195.9
313.15 0.8138 1197.0
313.15 0.8906 1197.8
313.15 0.9373 1198.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Speed of sound, m/s - Liquid
283.15 0.0448 1294.9
283.15 0.1051 1298.7
283.15 0.2010 1304.0
283.15 0.3026 1309.0
283.15 0.4115 1313.8
283.15 0.5038 1317.5
283.15 0.6065 1321.9
283.15 0.7044 1326.1
283.15 0.7888 1330.0
283.15 0.8925 1334.9
283.15 0.9533 1337.6
298.15 0.0471 1245.5
298.15 0.0972 1247.7
298.15 0.2026 1251.7
298.15 0.2903 1254.4
298.15 0.3266 1255.4
298.15 0.3987 1257.3
298.15 0.5146 1260.2
298.15 0.6077 1262.6
298.15 0.7128 1265.5
298.15 0.7996 1267.9
298.15 0.8595 1269.5
298.15 0.8915 1270.4
298.15 0.9350 1271.5
313.15 0.1081 1189.1
313.15 0.1937 1190.6
313.15 0.2954 1192.1
313.15 0.4021 1193.4
313.15 0.5032 1194.4
313.15 0.6035 1195.1
313.15 0.6615 1195.5
313.15 0.7114 1195.9
313.15 0.8138 1197.0
313.15 0.8906 1197.8
313.15 0.9373 1198.0

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 40.00 366.76
0.0000 53.33 373.74
0.0000 66.66 379.43
0.0000 79.99 384.26
0.0000 93.32 388.49
0.0000 98.66 390.04
0.0977 40.00 361.61
0.0977 53.33 369.07
0.0977 66.66 375.09
0.0977 79.99 380.16
0.0977 93.32 384.60
0.0977 98.66 386.24
0.1952 40.00 356.24
0.1952 53.33 364.14
0.1952 66.66 370.58
0.1952 79.99 375.96
0.1952 93.32 380.62
0.1952 98.66 382.31
0.2912 40.00 351.94
0.2912 53.33 360.08
0.2912 66.66 366.67
0.2912 79.99 372.17
0.2912 93.32 376.93
0.2912 98.66 378.71
0.3910 40.00 347.88
0.3910 53.33 356.20
0.3910 66.66 362.88
0.3910 79.99 368.52
0.3910 93.32 373.39
0.3910 98.66 375.22
0.4936 40.00 344.44
0.4936 53.33 352.72
0.4936 66.66 359.47
0.4936 79.99 365.17
0.4936 93.32 370.16
0.4936 98.66 371.99
0.6079 40.00 341.35
0.6079 53.33 349.64
0.6079 66.66 356.35
0.6079 79.99 362.06
0.6079 93.32 367.03
0.6079 98.66 368.86
0.7049 40.00 339.04
0.7049 53.33 347.23
0.7049 66.66 354.00
0.7049 79.99 359.68
0.7049 93.32 364.66
0.7049 98.66 366.48
0.8050 40.00 336.80
0.8050 53.33 344.99
0.8050 66.66 351.66
0.8050 79.99 357.35
0.8050 93.32 362.33
0.8050 98.66 364.17
0.9028 40.00 334.94
0.9028 53.33 343.07
0.9028 66.66 349.73
0.9028 79.99 355.41
0.9028 93.32 360.39
0.9028 98.66 362.23
0.9708 40.00 333.50
0.9708 53.33 341.61
0.9708 66.66 348.25
0.9708 79.99 353.91
0.9708 93.32 358.88
0.9708 98.66 360.71
1.0000 40.00 332.98
1.0000 53.33 341.09
1.0000 66.66 347.72
1.0000 79.99 353.38
1.0000 93.32 358.37
1.0000 98.66 360.22

Boiling temperature at pressure P, K [ref]

Fixed Measured
Mole fraction of Tetrahydropyran (1) - Liquid Pressure, kPa - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 40.00 366.76
0.0000 53.33 373.74
0.0000 66.66 379.43
0.0000 79.99 384.26
0.0000 93.32 388.49
0.0000 98.66 390.04
0.0977 40.00 361.61
0.0977 53.33 369.07
0.0977 66.66 375.09
0.0977 79.99 380.16
0.0977 93.32 384.60
0.0977 98.66 386.24
0.1952 40.00 356.24
0.1952 53.33 364.14
0.1952 66.66 370.58
0.1952 79.99 375.96
0.1952 93.32 380.62
0.1952 98.66 382.31
0.2912 40.00 351.94
0.2912 53.33 360.08
0.2912 66.66 366.67
0.2912 79.99 372.17
0.2912 93.32 376.93
0.2912 98.66 378.71
0.3910 40.00 347.88
0.3910 53.33 356.20
0.3910 66.66 362.88
0.3910 79.99 368.52
0.3910 93.32 373.39
0.3910 98.66 375.22
0.4936 40.00 344.44
0.4936 53.33 352.72
0.4936 66.66 359.47
0.4936 79.99 365.17
0.4936 93.32 370.16
0.4936 98.66 371.99
0.6079 40.00 341.35
0.6079 53.33 349.64
0.6079 66.66 356.35
0.6079 79.99 362.06
0.6079 93.32 367.03
0.6079 98.66 368.86
0.7049 40.00 339.04
0.7049 53.33 347.23
0.7049 66.66 354.00
0.7049 79.99 359.68
0.7049 93.32 364.66
0.7049 98.66 366.48
0.8050 40.00 336.80
0.8050 53.33 344.99
0.8050 66.66 351.66
0.8050 79.99 357.35
0.8050 93.32 362.33
0.8050 98.66 364.17
0.9028 40.00 334.94
0.9028 53.33 343.07
0.9028 66.66 349.73
0.9028 79.99 355.41
0.9028 93.32 360.39
0.9028 98.66 362.23
0.9708 40.00 333.50
0.9708 53.33 341.61
0.9708 66.66 348.25
0.9708 79.99 353.91
0.9708 93.32 358.88
0.9708 98.66 360.71
1.0000 40.00 332.98
1.0000 53.33 341.09
1.0000 66.66 347.72
1.0000 79.99 353.38
1.0000 93.32 358.37
1.0000 98.66 360.22

Sources