Mixture of Tetrahydropyran + o-Xylene

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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

o-Xylene

Name
o-Xylene
InChI
InChI=1S/C8H10/c1-7-5-3-4-6-8(7)2/h3-6H,1-2H3
InChI Key
CTQNGGLPUBDAKN-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccccc1C
Mol. Weight (g/mol)
106.17
CAS
95-47-6
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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 (1) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
298.15 0.0918 184.41
298.15 0.1317 183.03
298.15 0.1765 181.48
298.15 0.5518 167.88
298.15 0.5871 166.53
298.15 0.6218 165.19
298.15 0.2108 180.29
298.15 0.2543 178.76
298.15 0.2876 177.59
298.15 0.3105 176.77
298.15 0.3651 174.81
298.15 0.4187 172.86
298.15 0.4498 171.71
298.15 0.4910 170.18
298.15 0.5217 169.03
298.15 0.6617 163.62
298.15 0.6901 162.50
298.15 0.7219 161.23
298.15 0.7561 159.85
298.15 0.7918 158.39
298.15 0.8231 157.11
298.15 0.8651 155.36
298.15 0.8902 154.31
298.15 0.9234 152.90
303.15 0.0918 186.00
303.15 0.1317 184.64
303.15 0.1765 183.10
303.15 0.2108 181.92
303.15 0.2543 180.40
303.15 0.2876 179.23
303.15 0.3105 178.42
303.15 0.3651 176.47
303.15 0.4187 174.53
303.15 0.4498 173.38
303.15 0.4910 171.85
303.15 0.5217 170.70
303.15 0.5518 169.56
303.15 0.5871 168.20
303.15 0.6218 166.86
303.15 0.6617 165.29
303.15 0.6901 164.16
303.15 0.7219 162.89
303.15 0.7561 161.50
303.15 0.7918 160.04
303.15 0.8231 158.75
303.15 0.8651 156.99
303.15 0.8902 155.93
303.15 0.9234 154.52
308.15 0.0918 187.56
308.15 0.1317 186.23
308.15 0.1765 184.72
308.15 0.2108 183.55
308.15 0.2543 182.06
308.15 0.2876 180.91
308.15 0.3105 180.11
308.15 0.3651 178.18
308.15 0.5518 171.34
308.15 0.5871 170.00
308.15 0.6218 168.66
308.15 0.6617 167.10
308.15 0.6901 165.98
308.15 0.7219 164.71
308.15 0.7561 163.33
308.15 0.7918 161.87
308.15 0.4187 176.26
308.15 0.4498 175.13
308.15 0.4910 173.62
308.15 0.5217 172.47
308.15 0.8231 160.58
308.15 0.8651 158.83
308.15 0.8902 157.78
308.15 0.9234 156.37

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 (1) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
298.15 0.0918 184.41
298.15 0.1317 183.03
298.15 0.1765 181.48
298.15 0.5518 167.88
298.15 0.5871 166.53
298.15 0.6218 165.19
298.15 0.2108 180.29
298.15 0.2543 178.76
298.15 0.2876 177.59
298.15 0.3105 176.77
298.15 0.3651 174.81
298.15 0.4187 172.86
298.15 0.4498 171.71
298.15 0.4910 170.18
298.15 0.5217 169.03
298.15 0.6617 163.62
298.15 0.6901 162.50
298.15 0.7219 161.23
298.15 0.7561 159.85
298.15 0.7918 158.39
298.15 0.8231 157.11
298.15 0.8651 155.36
298.15 0.8902 154.31
298.15 0.9234 152.90
303.15 0.0918 186.00
303.15 0.1317 184.64
303.15 0.1765 183.10
303.15 0.2108 181.92
303.15 0.2543 180.40
303.15 0.2876 179.23
303.15 0.3105 178.42
303.15 0.3651 176.47
303.15 0.4187 174.53
303.15 0.4498 173.38
303.15 0.4910 171.85
303.15 0.5217 170.70
303.15 0.5518 169.56
303.15 0.5871 168.20
303.15 0.6218 166.86
303.15 0.6617 165.29
303.15 0.6901 164.16
303.15 0.7219 162.89
303.15 0.7561 161.50
303.15 0.7918 160.04
303.15 0.8231 158.75
303.15 0.8651 156.99
303.15 0.8902 155.93
303.15 0.9234 154.52
308.15 0.0918 187.56
308.15 0.1317 186.23
308.15 0.1765 184.72
308.15 0.2108 183.55
308.15 0.2543 182.06
308.15 0.2876 180.91
308.15 0.3105 180.11
308.15 0.3651 178.18
308.15 0.5518 171.34
308.15 0.5871 170.00
308.15 0.6218 168.66
308.15 0.6617 167.10
308.15 0.6901 165.98
308.15 0.7219 164.71
308.15 0.7561 163.33
308.15 0.7918 161.87
308.15 0.4187 176.26
308.15 0.4498 175.13
308.15 0.4910 173.62
308.15 0.5217 172.47
308.15 0.8231 160.58
308.15 0.8651 158.83
308.15 0.8902 157.78
308.15 0.9234 156.37

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

Operational conditions:

Mole fraction of Tetrahydropyran (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0587 -0.0266
0.0691 -0.0305
0.0838 -0.0356
0.1451 -0.0516
0.1809 -0.0573
0.2454 -0.0613
0.3023 -0.0588
0.3872 -0.0465
0.4425 -0.0342
0.5752 0.0024
0.6470 0.0220
0.7443 0.0421
0.8495 0.0467
0.9437 0.0267

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

Operational conditions:

Mole fraction of Tetrahydropyran (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0587 -0.0266
0.0691 -0.0305
0.0838 -0.0356
0.1451 -0.0516
0.1809 -0.0573
0.2454 -0.0613
0.3023 -0.0588
0.3872 -0.0465
0.4425 -0.0342
0.5752 0.0024
0.6470 0.0220
0.7443 0.0421
0.8495 0.0467
0.9437 0.0267

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0908 876.43
298.15 0.1432 876.68
298.15 0.1897 876.87
298.15 0.2318 877.04
298.15 0.2953 877.26
298.15 0.3310 877.39
298.15 0.3872 877.57
298.15 0.4287 877.7
298.15 0.4792 877.86
298.15 0.5187 877.99
298.15 0.5725 878.16
298.15 0.6182 878.31
298.15 0.6682 878.47
298.15 0.7187 878.62
298.15 0.7729 878.78
298.15 0.8367 878.94
298.15 0.8952 879.05
298.15 0.9274 879.1
303.15 0.0908 872.06
303.15 0.1432 872.25
303.15 0.1897 872.4
303.15 0.2318 872.53
303.15 0.2953 872.71
303.15 0.3310 872.81
303.15 0.3872 872.95
303.15 0.4287 873.05
303.15 0.4792 873.17
303.15 0.5187 873.26
303.15 0.5725 873.38
303.15 0.6182 873.48
303.15 0.6682 873.58
303.15 0.7187 873.67
303.15 0.7729 873.77
303.15 0.8367 873.86
303.15 0.8952 873.93
303.15 0.9274 873.96

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0908 876.43
298.15 0.1432 876.68
298.15 0.1897 876.87
298.15 0.2318 877.04
298.15 0.2953 877.26
298.15 0.3310 877.39
298.15 0.3872 877.57
298.15 0.4287 877.7
298.15 0.4792 877.86
298.15 0.5187 877.99
298.15 0.5725 878.16
298.15 0.6182 878.31
298.15 0.6682 878.47
298.15 0.7187 878.62
298.15 0.7729 878.78
298.15 0.8367 878.94
298.15 0.8952 879.05
298.15 0.9274 879.1
303.15 0.0908 872.06
303.15 0.1432 872.25
303.15 0.1897 872.4
303.15 0.2318 872.53
303.15 0.2953 872.71
303.15 0.3310 872.81
303.15 0.3872 872.95
303.15 0.4287 873.05
303.15 0.4792 873.17
303.15 0.5187 873.26
303.15 0.5725 873.38
303.15 0.6182 873.48
303.15 0.6682 873.58
303.15 0.7187 873.67
303.15 0.7729 873.77
303.15 0.8367 873.86
303.15 0.8952 873.93
303.15 0.9274 873.96

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (1) - Liquid Speed of sound, m/s - Liquid
0.0854 1319.0
0.1494 1315.0
0.2134 1309.0
0.2834 1303.0
0.3778 1293.0
0.4756 1281.0
0.5132 1277.0
0.5668 1270.0
0.6124 1265.0
0.7035 1254.0
0.7866 1245.0
0.8645 1237.0
0.9344 1230.0
0.9545 1228.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Speed of sound, m/s - Liquid
298.15 0.0908 1345.3
298.15 0.1432 1343.1
298.15 0.1897 1340.4
298.15 0.2318 1337.4
298.15 0.2953 1332.1
298.15 0.3310 1328.8
298.15 0.3872 1323.2
298.15 0.4287 1319.0
298.15 0.4792 1313.7
298.15 0.5187 1309.6
298.15 0.5725 1304.1
298.15 0.6182 1299.5
298.15 0.6682 1294.6
298.15 0.7187 1290.0
298.15 0.7729 1285.3
298.15 0.8367 1280.2
298.15 0.8952 1276.1
298.15 0.9274 1274.0
303.15 0.0908 1323.7
303.15 0.1432 1321.0
303.15 0.1897 1317.9
303.15 0.2318 1314.7
303.15 0.2953 1309.2
303.15 0.3310 1305.9
303.15 0.3872 1300.4
303.15 0.4287 1296.2
303.15 0.4792 1291.0
303.15 0.5187 1286.9
303.15 0.5725 1281.4
303.15 0.6182 1276.8
303.15 0.6682 1272.0
303.15 0.7187 1267.3
303.15 0.7729 1262.5
303.15 0.8367 1257.3
303.15 0.8952 1253.1
303.15 0.9274 1251.0

Speed of sound, m/s [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (1) - Liquid Speed of sound, m/s - Liquid
0.0854 1319.0
0.1494 1315.0
0.2134 1309.0
0.2834 1303.0
0.3778 1293.0
0.4756 1281.0
0.5132 1277.0
0.5668 1270.0
0.6124 1265.0
0.7035 1254.0
0.7866 1245.0
0.8645 1237.0
0.9344 1230.0
0.9545 1228.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydropyran (1) - Liquid Speed of sound, m/s - Liquid
298.15 0.0908 1345.3
298.15 0.1432 1343.1
298.15 0.1897 1340.4
298.15 0.2318 1337.4
298.15 0.2953 1332.1
298.15 0.3310 1328.8
298.15 0.3872 1323.2
298.15 0.4287 1319.0
298.15 0.4792 1313.7
298.15 0.5187 1309.6
298.15 0.5725 1304.1
298.15 0.6182 1299.5
298.15 0.6682 1294.6
298.15 0.7187 1290.0
298.15 0.7729 1285.3
298.15 0.8367 1280.2
298.15 0.8952 1276.1
298.15 0.9274 1274.0
303.15 0.0908 1323.7
303.15 0.1432 1321.0
303.15 0.1897 1317.9
303.15 0.2318 1314.7
303.15 0.2953 1309.2
303.15 0.3310 1305.9
303.15 0.3872 1300.4
303.15 0.4287 1296.2
303.15 0.4792 1291.0
303.15 0.5187 1286.9
303.15 0.5725 1281.4
303.15 0.6182 1276.8
303.15 0.6682 1272.0
303.15 0.7187 1267.3
303.15 0.7729 1262.5
303.15 0.8367 1257.3
303.15 0.8952 1253.1
303.15 0.9274 1251.0

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0536 -1.2000e-08
0.0643 -1.4000e-08
0.0805 -1.7000e-08
0.1127 -2.3000e-08
0.1816 -3.4000e-08
0.2975 -4.7000e-08
0.3954 -5.3000e-08
0.4935 -5.5000e-08
0.5200 -5.4000e-08
0.5642 -5.3000e-08
0.6421 -4.8000e-08
0.7314 -4.0000e-08
0.8832 -1.9000e-08
0.9228 -1.3000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Tetrahydropyran (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0536 -1.2000e-08
0.0643 -1.4000e-08
0.0805 -1.7000e-08
0.1127 -2.3000e-08
0.1816 -3.4000e-08
0.2975 -4.7000e-08
0.3954 -5.3000e-08
0.4935 -5.5000e-08
0.5200 -5.4000e-08
0.5642 -5.3000e-08
0.6421 -4.8000e-08
0.7314 -4.0000e-08
0.8832 -1.9000e-08
0.9228 -1.3000e-08

Sources