Mixture of Toluene + Tetrahydropyran

Excel

Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

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 0.0937 157.00
298.15 0.1369 156.86
298.15 0.1932 156.64
298.15 0.2308 156.46
298.15 0.2894 156.15
298.15 0.3187 155.98
298.15 0.3507 155.79
298.15 0.3916 155.52
298.15 0.4206 155.32
298.15 0.4618 155.02
298.15 0.4906 154.81
298.15 0.5137 154.63
298.15 0.5517 154.32
298.15 0.5907 154.00
298.15 0.6208 153.74
298.15 0.6623 153.37
298.15 0.6987 153.03
298.15 0.7135 152.89
298.15 0.7510 152.52
298.15 0.7917 152.10
298.15 0.8246 151.75
298.15 0.8516 151.45
298.15 0.8914 150.99
298.15 0.9123 150.74
303.15 0.0937 158.50
303.15 0.1369 158.39
303.15 0.1932 158.18
303.15 0.2308 158.01
303.15 0.2894 157.71
303.15 0.3187 157.54
303.15 0.3507 157.35
303.15 0.3916 157.09
303.15 0.4206 156.90
303.15 0.4618 156.61
303.15 0.4906 156.40
303.15 0.5137 156.23
303.15 0.5517 155.94
303.15 0.5907 155.62
303.15 0.6208 155.38
303.15 0.6623 155.02
303.15 0.6987 154.69
303.15 0.7135 154.56
303.15 0.7510 154.20
303.15 0.7917 153.79
303.15 0.8246 153.44
303.15 0.8516 153.14
303.15 0.8914 152.67
303.15 0.9123 152.41
308.15 0.0937 160.08
308.15 0.1369 159.99
308.15 0.1932 159.81
308.15 0.2308 159.65
308.15 0.2894 159.37
308.15 0.3187 159.22
308.15 0.3507 159.04
308.15 0.3916 158.79
308.15 0.4206 158.61
308.15 0.4618 158.34
308.15 0.4906 158.14
308.15 0.5137 157.98
308.15 0.5517 157.71
308.15 0.5907 157.42
308.15 0.6208 157.19
308.15 0.6623 156.86
308.15 0.6987 156.55
308.15 0.7135 156.42
308.15 0.7510 156.08
308.15 0.7917 155.68
308.15 0.8246 155.34
308.15 0.8516 155.05
308.15 0.8914 154.58
308.15 0.9123 154.32

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 0.0937 157.00
298.15 0.1369 156.86
298.15 0.1932 156.64
298.15 0.2308 156.46
298.15 0.2894 156.15
298.15 0.3187 155.98
298.15 0.3507 155.79
298.15 0.3916 155.52
298.15 0.4206 155.32
298.15 0.4618 155.02
298.15 0.4906 154.81
298.15 0.5137 154.63
298.15 0.5517 154.32
298.15 0.5907 154.00
298.15 0.6208 153.74
298.15 0.6623 153.37
298.15 0.6987 153.03
298.15 0.7135 152.89
298.15 0.7510 152.52
298.15 0.7917 152.10
298.15 0.8246 151.75
298.15 0.8516 151.45
298.15 0.8914 150.99
298.15 0.9123 150.74
303.15 0.0937 158.50
303.15 0.1369 158.39
303.15 0.1932 158.18
303.15 0.2308 158.01
303.15 0.2894 157.71
303.15 0.3187 157.54
303.15 0.3507 157.35
303.15 0.3916 157.09
303.15 0.4206 156.90
303.15 0.4618 156.61
303.15 0.4906 156.40
303.15 0.5137 156.23
303.15 0.5517 155.94
303.15 0.5907 155.62
303.15 0.6208 155.38
303.15 0.6623 155.02
303.15 0.6987 154.69
303.15 0.7135 154.56
303.15 0.7510 154.20
303.15 0.7917 153.79
303.15 0.8246 153.44
303.15 0.8516 153.14
303.15 0.8914 152.67
303.15 0.9123 152.41
308.15 0.0937 160.08
308.15 0.1369 159.99
308.15 0.1932 159.81
308.15 0.2308 159.65
308.15 0.2894 159.37
308.15 0.3187 159.22
308.15 0.3507 159.04
308.15 0.3916 158.79
308.15 0.4206 158.61
308.15 0.4618 158.34
308.15 0.4906 158.14
308.15 0.5137 157.98
308.15 0.5517 157.71
308.15 0.5907 157.42
308.15 0.6208 157.19
308.15 0.6623 156.86
308.15 0.6987 156.55
308.15 0.7135 156.42
308.15 0.7510 156.08
308.15 0.7917 155.68
308.15 0.8246 155.34
308.15 0.8516 155.05
308.15 0.8914 154.58
308.15 0.9123 154.32

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
0.0445 -0.0285
0.0662 -0.0427
0.0837 -0.0541
0.1138 -0.0737
0.2154 -0.1354
0.2806 -0.1687
0.3031 -0.1787
0.3970 -0.2101
0.5319 -0.2225
0.6305 -0.2058
0.7413 -0.1629
0.8325 -0.1121
0.9352 -0.0445
0.9727 -0.0187

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
0.0445 -0.0285
0.0662 -0.0427
0.0837 -0.0541
0.1138 -0.0737
0.2154 -0.1354
0.2806 -0.1687
0.3031 -0.1787
0.3970 -0.2101
0.5319 -0.2225
0.6305 -0.2058
0.7413 -0.1629
0.8325 -0.1121
0.9352 -0.0445
0.9727 -0.0187

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 0.0834 863.93
298.15 0.1245 864.77
298.15 0.1765 865.79
298.15 0.2387 866.99
298.15 0.3017 868.16
298.15 0.3541 869.11
298.15 0.4098 870.1
298.15 0.4467 870.74
298.15 0.4915 871.51
298.15 0.5487 872.47
298.15 0.6008 873.33
298.15 0.6472 874.08
298.15 0.6954 874.84
298.15 0.7321 875.41
298.15 0.7832 876.18
298.15 0.8241 876.78
298.15 0.8937 877.76
298.15 0.9205 878.12
303.15 0.0834 859.19
303.15 0.1245 859.99
303.15 0.1765 860.99
303.15 0.2387 862.15
303.15 0.3017 863.3
303.15 0.3541 864.23
303.15 0.4098 865.2
303.15 0.4467 865.83
303.15 0.4915 866.59
303.15 0.5487 867.53
303.15 0.6008 868.36
303.15 0.6472 869.09
303.15 0.6954 869.83
303.15 0.7321 870.38
303.15 0.7832 871.13
303.15 0.8241 871.71
303.15 0.8937 872.65
303.15 0.9205 873.0

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 0.0834 863.93
298.15 0.1245 864.77
298.15 0.1765 865.79
298.15 0.2387 866.99
298.15 0.3017 868.16
298.15 0.3541 869.11
298.15 0.4098 870.1
298.15 0.4467 870.74
298.15 0.4915 871.51
298.15 0.5487 872.47
298.15 0.6008 873.33
298.15 0.6472 874.08
298.15 0.6954 874.84
298.15 0.7321 875.41
298.15 0.7832 876.18
298.15 0.8241 876.78
298.15 0.8937 877.76
298.15 0.9205 878.12
303.15 0.0834 859.19
303.15 0.1245 859.99
303.15 0.1765 860.99
303.15 0.2387 862.15
303.15 0.3017 863.3
303.15 0.3541 864.23
303.15 0.4098 865.2
303.15 0.4467 865.83
303.15 0.4915 866.59
303.15 0.5487 867.53
303.15 0.6008 868.36
303.15 0.6472 869.09
303.15 0.6954 869.83
303.15 0.7321 870.38
303.15 0.7832 871.13
303.15 0.8241 871.71
303.15 0.8937 872.65
303.15 0.9205 873.0

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Speed of sound, m/s - Liquid
0.0925 1259.0
0.1343 1258.0
0.1789 1257.0
0.2587 1256.0
0.3742 1254.0
0.4263 1253.0
0.4815 1251.0
0.5187 1250.0
0.5795 1248.0
0.6765 1243.0
0.7122 1242.0
0.7646 1239.0
0.8487 1234.0
0.9252 1229.0

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 0.0834 1303.2
298.15 0.1245 1302.3
298.15 0.1765 1301.2
298.15 0.2387 1299.7
298.15 0.3017 1298.1
298.15 0.3541 1296.6
298.15 0.4098 1295.0
298.15 0.4467 1293.9
298.15 0.4915 1292.5
298.15 0.5487 1290.6
298.15 0.6008 1288.8
298.15 0.6472 1287.1
298.15 0.6954 1285.2
298.15 0.7321 1283.7
298.15 0.7832 1281.5
298.15 0.8241 1279.6
298.15 0.8937 1276.1
298.15 0.9205 1274.6
303.15 0.0834 1281.1
303.15 0.1245 1280.0
303.15 0.1765 1278.7
303.15 0.2387 1277.1
303.15 0.3017 1275.3
303.15 0.3541 1273.8
303.15 0.4098 1272.2
303.15 0.4467 1271.0
303.15 0.4915 1269.5
303.15 0.5487 1267.5
303.15 0.6008 1265.6
303.15 0.6472 1263.7
303.15 0.6954 1261.8
303.15 0.7321 1260.2
303.15 0.7832 1257.9
303.15 0.8241 1255.9
303.15 0.8937 1252.5
303.15 0.9205 1251.1

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Speed of sound, m/s - Liquid
0.0925 1259.0
0.1343 1258.0
0.1789 1257.0
0.2587 1256.0
0.3742 1254.0
0.4263 1253.0
0.4815 1251.0
0.5187 1250.0
0.5795 1248.0
0.6765 1243.0
0.7122 1242.0
0.7646 1239.0
0.8487 1234.0
0.9252 1229.0

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 0.0834 1303.2
298.15 0.1245 1302.3
298.15 0.1765 1301.2
298.15 0.2387 1299.7
298.15 0.3017 1298.1
298.15 0.3541 1296.6
298.15 0.4098 1295.0
298.15 0.4467 1293.9
298.15 0.4915 1292.5
298.15 0.5487 1290.6
298.15 0.6008 1288.8
298.15 0.6472 1287.1
298.15 0.6954 1285.2
298.15 0.7321 1283.7
298.15 0.7832 1281.5
298.15 0.8241 1279.6
298.15 0.8937 1276.1
298.15 0.9205 1274.6
303.15 0.0834 1281.1
303.15 0.1245 1280.0
303.15 0.1765 1278.7
303.15 0.2387 1277.1
303.15 0.3017 1275.3
303.15 0.3541 1273.8
303.15 0.4098 1272.2
303.15 0.4467 1271.0
303.15 0.4915 1269.5
303.15 0.5487 1267.5
303.15 0.6008 1265.6
303.15 0.6472 1263.7
303.15 0.6954 1261.8
303.15 0.7321 1260.2
303.15 0.7832 1257.9
303.15 0.8241 1255.9
303.15 0.8937 1252.5
303.15 0.9205 1251.1

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0554 -3.1000e-08
0.0673 -3.7000e-08
0.0850 -4.6000e-08
0.1534 -7.9000e-08
0.1861 -9.2000e-08
0.2311 -1.1000e-07
0.2942 -1.2900e-07
0.4109 -1.5300e-07
0.5273 -1.5900e-07
0.6433 -1.4600e-07
0.7215 -1.2700e-07
0.8202 -9.3000e-08
0.9297 -4.0000e-08
0.9735 -1.6000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (2) - Liquid Excess molar volume, m3/mol - Liquid
0.0554 -3.1000e-08
0.0673 -3.7000e-08
0.0850 -4.6000e-08
0.1534 -7.9000e-08
0.1861 -9.2000e-08
0.2311 -1.1000e-07
0.2942 -1.2900e-07
0.4109 -1.5300e-07
0.5273 -1.5900e-07
0.6433 -1.4600e-07
0.7215 -1.2700e-07
0.8202 -9.3000e-08
0.9297 -4.0000e-08
0.9735 -1.6000e-08

Sources