Mixture of Benzene + Tetrahydropyran

Excel

Benzene

Name
Benzene
InChI
InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
InChI Key
UHOVQNZJYSORNB-UHFFFAOYSA-N
Formula
C6H6
SMILES
c1ccccc1
Mol. Weight (g/mol)
78.11
CAS
71-43-2

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
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Datasets

  1. Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. ρl - Mass density, kg/m3 (2)
  4. csound,fluid - Speed of Sound, m/s (4)
  5. Excess molar volume, m3/mol (2)

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (2) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
298.15 0.0859 136.89
298.15 0.1279 137.71
298.15 0.1598 138.32
298.15 0.1982 139.05
298.15 0.2254 139.56
298.15 0.2657 140.30
298.15 0.3017 140.94
298.15 0.3509 141.80
298.15 0.3898 142.45
298.15 0.4176 142.91
298.15 0.4428 143.31
298.15 0.4987 144.17
298.15 0.5234 144.54
298.15 0.5592 145.05
298.15 0.5983 145.58
298.15 0.6132 145.78
298.15 0.6478 146.23
298.15 0.6876 146.71
298.15 0.7231 147.12
298.15 0.7623 147.55
298.15 0.7905 147.85
298.15 0.8217 148.15
298.15 0.8507 148.43
298.15 0.9003 148.86
303.15 0.0859 138.21
303.15 0.1279 139.06
303.15 0.1598 139.70
303.15 0.1982 140.45
303.15 0.2254 140.97
303.15 0.2657 141.72
303.15 0.3017 142.38
303.15 0.3509 143.26
303.15 0.5234 146.08
303.15 0.5592 146.61
303.15 0.5983 147.17
303.15 0.6132 147.37
303.15 0.6478 147.84
303.15 0.6876 148.35
303.15 0.7231 148.78
303.15 0.7623 149.22
303.15 0.3898 143.93
303.15 0.4176 144.39
303.15 0.4428 144.81
303.15 0.4987 145.70
303.15 0.7905 149.53
303.15 0.8217 149.84
303.15 0.8507 150.12
303.15 0.9003 150.54
308.15 0.0859 139.54
308.15 0.1279 140.44
308.15 0.1598 141.10
308.15 0.1982 141.88
308.15 0.2254 142.43
308.15 0.2657 143.21
308.15 0.3017 143.89
308.15 0.3509 144.80
308.15 0.3898 145.50
308.15 0.4176 145.99
308.15 0.4428 146.42
308.15 0.4987 147.36
308.15 0.5234 147.76
308.15 0.5592 148.32
308.15 0.5983 148.91
308.15 0.6132 149.13
308.15 0.6478 149.63
308.15 0.6876 150.17
308.15 0.7231 150.63
308.15 0.7623 151.10
308.15 0.7905 151.42
308.15 0.8217 151.75
308.15 0.8507 152.04
308.15 0.9003 152.47

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (2) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
298.15 0.0859 136.89
298.15 0.1279 137.71
298.15 0.1598 138.32
298.15 0.1982 139.05
298.15 0.2254 139.56
298.15 0.2657 140.30
298.15 0.3017 140.94
298.15 0.3509 141.80
298.15 0.3898 142.45
298.15 0.4176 142.91
298.15 0.4428 143.31
298.15 0.4987 144.17
298.15 0.5234 144.54
298.15 0.5592 145.05
298.15 0.5983 145.58
298.15 0.6132 145.78
298.15 0.6478 146.23
298.15 0.6876 146.71
298.15 0.7231 147.12
298.15 0.7623 147.55
298.15 0.7905 147.85
298.15 0.8217 148.15
298.15 0.8507 148.43
298.15 0.9003 148.86
303.15 0.0859 138.21
303.15 0.1279 139.06
303.15 0.1598 139.70
303.15 0.1982 140.45
303.15 0.2254 140.97
303.15 0.2657 141.72
303.15 0.3017 142.38
303.15 0.3509 143.26
303.15 0.5234 146.08
303.15 0.5592 146.61
303.15 0.5983 147.17
303.15 0.6132 147.37
303.15 0.6478 147.84
303.15 0.6876 148.35
303.15 0.7231 148.78
303.15 0.7623 149.22
303.15 0.3898 143.93
303.15 0.4176 144.39
303.15 0.4428 144.81
303.15 0.4987 145.70
303.15 0.7905 149.53
303.15 0.8217 149.84
303.15 0.8507 150.12
303.15 0.9003 150.54
308.15 0.0859 139.54
308.15 0.1279 140.44
308.15 0.1598 141.10
308.15 0.1982 141.88
308.15 0.2254 142.43
308.15 0.2657 143.21
308.15 0.3017 143.89
308.15 0.3509 144.80
308.15 0.3898 145.50
308.15 0.4176 145.99
308.15 0.4428 146.42
308.15 0.4987 147.36
308.15 0.5234 147.76
308.15 0.5592 148.32
308.15 0.5983 148.91
308.15 0.6132 149.13
308.15 0.6478 149.63
308.15 0.6876 150.17
308.15 0.7231 150.63
308.15 0.7623 151.10
308.15 0.7905 151.42
308.15 0.8217 151.75
308.15 0.8507 152.04
308.15 0.9003 152.47

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

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0484 -0.0326
0.0757 -0.0516
0.0978 -0.0671
0.1432 -0.0985
0.2425 -0.1608
0.3110 -0.1952
0.3850 -0.2216
0.4982 -0.2365
0.6013 -0.2220
0.6875 -0.1909
0.7073 -0.1816
0.7832 -0.1399
0.8501 -0.0974
0.9230 -0.0488

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

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0484 -0.0326
0.0757 -0.0516
0.0978 -0.0671
0.1432 -0.0985
0.2425 -0.1608
0.3110 -0.1952
0.3850 -0.2216
0.4982 -0.2365
0.6013 -0.2220
0.6875 -0.1909
0.7073 -0.1816
0.7832 -0.1399
0.8501 -0.0974
0.9230 -0.0488

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0789 874.6
298.15 0.1324 875.21
298.15 0.1784 875.68
298.15 0.2239 876.1
298.15 0.2876 876.63
298.15 0.3276 876.92
298.15 0.3769 877.26
298.15 0.4285 877.58
298.15 0.4794 877.87
298.15 0.5598 878.27
298.15 0.6024 878.46
298.15 0.6534 878.66
298.15 0.7006 878.82
298.15 0.7432 878.95
298.15 0.7943 879.07
298.15 0.8213 879.12
298.15 0.8763 879.18
298.15 0.9148 879.2
303.15 0.0789 869.25
303.15 0.1324 869.87
303.15 0.1784 870.35
303.15 0.2239 870.78
303.15 0.2876 871.32
303.15 0.3276 871.63
303.15 0.3769 871.97
303.15 0.4285 872.3
303.15 0.4794 872.59
303.15 0.5598 872.99
303.15 0.6024 873.17
303.15 0.6534 873.37
303.15 0.7006 873.53
303.15 0.7432 873.65
303.15 0.7943 873.77
303.15 0.8213 873.83
303.15 0.8763 873.92
303.15 0.9148 873.96

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (2) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0789 874.6
298.15 0.1324 875.21
298.15 0.1784 875.68
298.15 0.2239 876.1
298.15 0.2876 876.63
298.15 0.3276 876.92
298.15 0.3769 877.26
298.15 0.4285 877.58
298.15 0.4794 877.87
298.15 0.5598 878.27
298.15 0.6024 878.46
298.15 0.6534 878.66
298.15 0.7006 878.82
298.15 0.7432 878.95
298.15 0.7943 879.07
298.15 0.8213 879.12
298.15 0.8763 879.18
298.15 0.9148 879.2
303.15 0.0789 869.25
303.15 0.1324 869.87
303.15 0.1784 870.35
303.15 0.2239 870.78
303.15 0.2876 871.32
303.15 0.3276 871.63
303.15 0.3769 871.97
303.15 0.4285 872.3
303.15 0.4794 872.59
303.15 0.5598 872.99
303.15 0.6024 873.17
303.15 0.6534 873.37
303.15 0.7006 873.53
303.15 0.7432 873.65
303.15 0.7943 873.77
303.15 0.8213 873.83
303.15 0.8763 873.92
303.15 0.9148 873.96

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Speed of sound, m/s - Liquid
0.0555 1256.0
0.1165 1253.0
0.1472 1251.0
0.2223 1248.0
0.2728 1246.0
0.3751 1241.0
0.4395 1239.0
0.4821 1237.0
0.5313 1238.0
0.6223 1233.0
0.6810 1231.0
0.7321 1230.0
0.8253 1228.0
0.9123 1226.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0789 1298.9
298.15 0.1324 1298.2
298.15 0.1784 1297.5
298.15 0.2239 1296.6
298.15 0.2876 1295.2
298.15 0.3276 1294.2
298.15 0.3769 1292.9
298.15 0.4285 1291.4
298.15 0.4794 1289.8
298.15 0.5598 1287.2
298.15 0.6024 1285.8
298.15 0.6534 1284.0
298.15 0.7006 1282.3
298.15 0.7432 1280.7
298.15 0.7943 1278.8
298.15 0.8213 1277.7
298.15 0.8763 1275.4
298.15 0.9148 1273.7
303.15 0.0789 1274.0
303.15 0.1324 1272.5
303.15 0.1784 1271.2
303.15 0.2239 1269.8
303.15 0.2876 1267.9
303.15 0.3276 1266.7
303.15 0.3769 1265.2
303.15 0.4285 1263.6
303.15 0.4794 1262.0
303.15 0.5598 1259.6
303.15 0.6024 1258.3
303.15 0.6534 1256.9
303.15 0.7006 1255.5
303.15 0.7432 1254.2
303.15 0.7943 1252.8
303.15 0.8213 1252.0
303.15 0.8763 1250.4
303.15 0.9148 1249.3

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Speed of sound, m/s - Liquid
0.0555 1256.0
0.1165 1253.0
0.1472 1251.0
0.2223 1248.0
0.2728 1246.0
0.3751 1241.0
0.4395 1239.0
0.4821 1237.0
0.5313 1238.0
0.6223 1233.0
0.6810 1231.0
0.7321 1230.0
0.8253 1228.0
0.9123 1226.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (2) - Liquid Speed of sound, m/s - Liquid
298.15 0.0789 1298.9
298.15 0.1324 1298.2
298.15 0.1784 1297.5
298.15 0.2239 1296.6
298.15 0.2876 1295.2
298.15 0.3276 1294.2
298.15 0.3769 1292.9
298.15 0.4285 1291.4
298.15 0.4794 1289.8
298.15 0.5598 1287.2
298.15 0.6024 1285.8
298.15 0.6534 1284.0
298.15 0.7006 1282.3
298.15 0.7432 1280.7
298.15 0.7943 1278.8
298.15 0.8213 1277.7
298.15 0.8763 1275.4
298.15 0.9148 1273.7
303.15 0.0789 1274.0
303.15 0.1324 1272.5
303.15 0.1784 1271.2
303.15 0.2239 1269.8
303.15 0.2876 1267.9
303.15 0.3276 1266.7
303.15 0.3769 1265.2
303.15 0.4285 1263.6
303.15 0.4794 1262.0
303.15 0.5598 1259.6
303.15 0.6024 1258.3
303.15 0.6534 1256.9
303.15 0.7006 1255.5
303.15 0.7432 1254.2
303.15 0.7943 1252.8
303.15 0.8213 1252.0
303.15 0.8763 1250.4
303.15 0.9148 1249.3

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0684 -4.9000e-08
0.1029 -6.9000e-08
0.1673 -1.0100e-07
0.1835 -1.0800e-07
0.2430 -1.2900e-07
0.3143 -1.4500e-07
0.4085 -1.5600e-07
0.5291 -1.5200e-07
0.5990 -1.4200e-07
0.6543 -1.3000e-07
0.7452 -1.0500e-07
0.7823 -9.3000e-08
0.8754 -5.7000e-08
0.9539 -2.3000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0684 -4.9000e-08
0.1029 -6.9000e-08
0.1673 -1.0100e-07
0.1835 -1.0800e-07
0.2430 -1.2900e-07
0.3143 -1.4500e-07
0.4085 -1.5600e-07
0.5291 -1.5200e-07
0.5990 -1.4200e-07
0.6543 -1.3000e-07
0.7452 -1.0500e-07
0.7823 -9.3000e-08
0.8754 -5.7000e-08
0.9539 -2.3000e-08

Sources