Mixture of Tetrahydropyran + Cyclohexanone

Datasets

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

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15	0.0995	176.32
293.15	0.1452	175.99
293.15	0.1965	175.76
293.15	0.2456	175.65
293.15	0.2863	175.47
293.15	0.3321	175.13
293.15	0.3845	174.53
293.15	0.4215	173.95
293.15	0.4723	172.86
293.15	0.5241	171.58
293.15	0.5796	169.75
293.15	0.6153	168.49
293.15	0.6654	166.35
293.15	0.7132	164.19
293.15	0.7698	161.26
293.15	0.8265	158.18
293.15	0.8732	155.48
293.15	0.9245	152.46
298.15	0.0995	178.62
298.15	0.1452	178.41
298.15	0.1965	178.40
298.15	0.2456	178.24
298.15	0.2863	178.06
298.15	0.3321	177.68
298.15	0.3845	177.03
298.15	0.4215	176.42
298.15	0.4723	175.29
298.15	0.5241	173.99
298.15	0.5796	172.22
298.15	0.6153	170.90
298.15	0.6654	168.77
298.15	0.7132	166.61
298.15	0.7698	163.68
298.15	0.8265	160.54
298.15	0.8732	157.76
298.15	0.9245	154.55
303.15	0.0995	180.90
303.15	0.1452	181.03
303.15	0.1965	181.02
303.15	0.2456	180.93
303.15	0.2863	180.64
303.15	0.3321	180.22
303.15	0.3845	179.51
303.15	0.4215	178.92
303.15	0.4723	177.75
303.15	0.5241	176.42
303.15	0.5796	174.56
303.15	0.6153	173.23
303.15	0.6654	171.21
303.15	0.7132	168.92
303.15	0.7698	165.99
303.15	0.8265	162.79
303.15	0.8732	159.90
303.15	0.9245	156.51
308.15	0.0995	183.36
308.15	0.1452	183.58
308.15	0.1965	183.49
308.15	0.2456	183.53
308.15	0.2863	183.30
308.15	0.3321	182.87
308.15	0.3845	182.09
308.15	0.4215	181.49
308.15	0.4723	180.31
308.15	0.5241	178.98
308.15	0.5796	177.13
308.15	0.6153	175.87
308.15	0.6654	173.73
308.15	0.7132	171.57
308.15	0.7698	168.56
308.15	0.8265	165.30
308.15	0.8732	162.31
308.15	0.9245	158.75

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

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15	0.0995	176.32
293.15	0.1452	175.99
293.15	0.1965	175.76
293.15	0.2456	175.65
293.15	0.2863	175.47
293.15	0.3321	175.13
293.15	0.3845	174.53
293.15	0.4215	173.95
293.15	0.4723	172.86
293.15	0.5241	171.58
293.15	0.5796	169.75
293.15	0.6153	168.49
293.15	0.6654	166.35
293.15	0.7132	164.19
293.15	0.7698	161.26
293.15	0.8265	158.18
293.15	0.8732	155.48
293.15	0.9245	152.46
298.15	0.0995	178.62
298.15	0.1452	178.41
298.15	0.1965	178.40
298.15	0.2456	178.24
298.15	0.2863	178.06
298.15	0.3321	177.68
298.15	0.3845	177.03
298.15	0.4215	176.42
298.15	0.4723	175.29
298.15	0.5241	173.99
298.15	0.5796	172.22
298.15	0.6153	170.90
298.15	0.6654	168.77
298.15	0.7132	166.61
298.15	0.7698	163.68
298.15	0.8265	160.54
298.15	0.8732	157.76
298.15	0.9245	154.55
303.15	0.0995	180.90
303.15	0.1452	181.03
303.15	0.1965	181.02
303.15	0.2456	180.93
303.15	0.2863	180.64
303.15	0.3321	180.22
303.15	0.3845	179.51
303.15	0.4215	178.92
303.15	0.4723	177.75
303.15	0.5241	176.42
303.15	0.5796	174.56
303.15	0.6153	173.23
303.15	0.6654	171.21
303.15	0.7132	168.92
303.15	0.7698	165.99
303.15	0.8265	162.79
303.15	0.8732	159.90
303.15	0.9245	156.51
308.15	0.0995	183.36
308.15	0.1452	183.58
308.15	0.1965	183.49
308.15	0.2456	183.53
308.15	0.2863	183.30
308.15	0.3321	182.87
308.15	0.3845	182.09
308.15	0.4215	181.49
308.15	0.4723	180.31
308.15	0.5241	178.98
308.15	0.5796	177.13
308.15	0.6153	175.87
308.15	0.6654	173.73
308.15	0.7132	171.57
308.15	0.7698	168.56
308.15	0.8265	165.30
308.15	0.8732	162.31
308.15	0.9245	158.75

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

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Temperature, K = 308.15 (Liquid)

Mole fraction of Tetrahydropyran (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0989	0.0410
0.1475	0.0584
0.1926	0.0712
0.2415	0.0860
0.2953	0.0968
0.3416	0.1058
0.3952	0.1120
0.4426	0.1148
0.4956	0.1155
0.5425	0.1135
0.5982	0.1075
0.6410	0.1021
0.6825	0.0948
0.7333	0.0835
0.7865	0.0697
0.8359	0.0553
0.8875	0.0389
0.9299	0.0241

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

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Temperature, K = 308.15 (Liquid)

Mole fraction of Tetrahydropyran (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0989	0.0410
0.1475	0.0584
0.1926	0.0712
0.2415	0.0860
0.2953	0.0968
0.3416	0.1058
0.3952	0.1120
0.4426	0.1148
0.4956	0.1155
0.5425	0.1135
0.5982	0.1075
0.6410	0.1021
0.6825	0.0948
0.7333	0.0835
0.7865	0.0697
0.8359	0.0553
0.8875	0.0389
0.9299	0.0241

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.1175	941.72
293.15	0.1586	939.66
293.15	0.1952	937.78
293.15	0.2471	935.05
293.15	0.2843	933.05
293.15	0.3396	930.0
293.15	0.3784	927.8
293.15	0.4178	925.53
293.15	0.4620	922.91
293.15	0.5009	920.56
293.15	0.5486	917.59
293.15	0.5814	915.51
293.15	0.6379	911.8
293.15	0.6899	908.28
293.15	0.7389	904.83
293.15	0.7804	901.82
293.15	0.8345	897.76
293.15	0.8929	893.19
298.15	0.1175	937.26
298.15	0.1586	935.2
298.15	0.1952	933.32
298.15	0.2471	930.59
298.15	0.2843	928.59
298.15	0.3396	925.53
298.15	0.3784	923.32
298.15	0.4178	921.03
298.15	0.4620	918.41
298.15	0.5009	916.03
298.15	0.5486	913.03
298.15	0.5814	910.91
298.15	0.6379	907.17
298.15	0.6899	903.58
298.15	0.7389	900.08
298.15	0.7804	897.02
298.15	0.8345	892.89
298.15	0.8929	888.23
303.15	0.1175	932.48
303.15	0.1586	930.42
303.15	0.1952	928.55
303.15	0.2471	925.82
303.15	0.2843	923.82
303.15	0.3396	920.76
303.15	0.3784	918.56
303.15	0.4178	916.26
303.15	0.4620	913.62
303.15	0.5009	911.24
303.15	0.5486	908.24
303.15	0.5814	906.13
303.15	0.6379	902.35
303.15	0.6899	898.75
303.15	0.7389	895.23
303.15	0.7804	892.14
303.15	0.8345	887.96
303.15	0.8929	883.23
308.15	0.1175	927.65
308.15	0.1586	925.6
308.15	0.1952	923.74
308.15	0.2471	921.01
308.15	0.2843	919.01
308.15	0.3396	915.96
308.15	0.3784	913.76
308.15	0.4178	911.46
308.15	0.4620	908.82
308.15	0.5009	906.44
308.15	0.5486	903.43
308.15	0.5814	901.31
308.15	0.6379	897.53
308.15	0.6899	893.91
308.15	0.7389	890.37
308.15	0.7804	887.26
308.15	0.8345	883.04
308.15	0.8929	878.25

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.1175	941.72
293.15	0.1586	939.66
293.15	0.1952	937.78
293.15	0.2471	935.05
293.15	0.2843	933.05
293.15	0.3396	930.0
293.15	0.3784	927.8
293.15	0.4178	925.53
293.15	0.4620	922.91
293.15	0.5009	920.56
293.15	0.5486	917.59
293.15	0.5814	915.51
293.15	0.6379	911.8
293.15	0.6899	908.28
293.15	0.7389	904.83
293.15	0.7804	901.82
293.15	0.8345	897.76
293.15	0.8929	893.19
298.15	0.1175	937.26
298.15	0.1586	935.2
298.15	0.1952	933.32
298.15	0.2471	930.59
298.15	0.2843	928.59
298.15	0.3396	925.53
298.15	0.3784	923.32
298.15	0.4178	921.03
298.15	0.4620	918.41
298.15	0.5009	916.03
298.15	0.5486	913.03
298.15	0.5814	910.91
298.15	0.6379	907.17
298.15	0.6899	903.58
298.15	0.7389	900.08
298.15	0.7804	897.02
298.15	0.8345	892.89
298.15	0.8929	888.23
303.15	0.1175	932.48
303.15	0.1586	930.42
303.15	0.1952	928.55
303.15	0.2471	925.82
303.15	0.2843	923.82
303.15	0.3396	920.76
303.15	0.3784	918.56
303.15	0.4178	916.26
303.15	0.4620	913.62
303.15	0.5009	911.24
303.15	0.5486	908.24
303.15	0.5814	906.13
303.15	0.6379	902.35
303.15	0.6899	898.75
303.15	0.7389	895.23
303.15	0.7804	892.14
303.15	0.8345	887.96
303.15	0.8929	883.23
308.15	0.1175	927.65
308.15	0.1586	925.6
308.15	0.1952	923.74
308.15	0.2471	921.01
308.15	0.2843	919.01
308.15	0.3396	915.96
308.15	0.3784	913.76
308.15	0.4178	911.46
308.15	0.4620	908.82
308.15	0.5009	906.44
308.15	0.5486	903.43
308.15	0.5814	901.31
308.15	0.6379	897.53
308.15	0.6899	893.91
308.15	0.7389	890.37
308.15	0.7804	887.26
308.15	0.8345	883.04
308.15	0.8929	878.25

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.1175	1411.4
293.15	0.1586	1404.6
293.15	0.1952	1398.7
293.15	0.2471	1390.5
293.15	0.2843	1384.6
293.15	0.3396	1376.1
293.15	0.3784	1370.3
293.15	0.4178	1364.5
293.15	0.4620	1358.2
293.15	0.5009	1352.6
293.15	0.5486	1346.1
293.15	0.5814	1341.7
293.15	0.6379	1334.3
293.15	0.6899	1327.7
293.15	0.7389	1321.7
293.15	0.7804	1316.8
293.15	0.8345	1310.6
293.15	0.8929	1304.1
298.15	0.1175	1394.5
298.15	0.1586	1387.3
298.15	0.1952	1381.0
298.15	0.2471	1372.1
298.15	0.2843	1365.8
298.15	0.3396	1356.7
298.15	0.3784	1350.6
298.15	0.4178	1344.5
298.15	0.4620	1337.8
298.15	0.5009	1332.1
298.15	0.5486	1325.3
298.15	0.5814	1320.7
298.15	0.6379	1313.2
298.15	0.6899	1306.4
298.15	0.7389	1299.7
298.15	0.7804	1294.6
298.15	0.8345	1288.1
298.15	0.8929	1281.4
303.15	0.1175	1373.6
303.15	0.1586	1366.3
303.15	0.1952	1359.7
303.15	0.2471	1350.7
303.15	0.2843	1344.4
303.15	0.3396	1335.2
303.15	0.3784	1328.9
303.15	0.4178	1322.6
303.15	0.4620	1315.8
303.15	0.5009	1309.9
303.15	0.5486	1302.9
303.15	0.5814	1298.2
303.15	0.6379	1290.3
303.15	0.6899	1283.4
303.15	0.7389	1277.0
303.15	0.7804	1271.8
303.15	0.8345	1265.3
303.15	0.8929	1258.5
308.15	0.1175	1353.2
308.15	0.1586	1345.6
308.15	0.1952	1339.1
308.15	0.2471	1329.8
308.15	0.2843	1323.4
308.15	0.3396	1314.0
308.15	0.3784	1307.6
308.15	0.4178	1301.2
308.15	0.4620	1294.2
308.15	0.5009	1288.3
308.15	0.5486	1281.1
308.15	0.5814	1276.3
308.15	0.6379	1268.3
308.15	0.6899	1261.3
308.15	0.7389	1254.8
308.15	0.7804	1249.6
308.15	0.8345	1242.9
308.15	0.8929	1236.1

Speed of sound, m/s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Frequency, MHz = 3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Tetrahydropyran (1) - Liquid	Speed of sound, m/s - Liquid
293.15	0.1175	1411.4
293.15	0.1586	1404.6
293.15	0.1952	1398.7
293.15	0.2471	1390.5
293.15	0.2843	1384.6
293.15	0.3396	1376.1
293.15	0.3784	1370.3
293.15	0.4178	1364.5
293.15	0.4620	1358.2
293.15	0.5009	1352.6
293.15	0.5486	1346.1
293.15	0.5814	1341.7
293.15	0.6379	1334.3
293.15	0.6899	1327.7
293.15	0.7389	1321.7
293.15	0.7804	1316.8
293.15	0.8345	1310.6
293.15	0.8929	1304.1
298.15	0.1175	1394.5
298.15	0.1586	1387.3
298.15	0.1952	1381.0
298.15	0.2471	1372.1
298.15	0.2843	1365.8
298.15	0.3396	1356.7
298.15	0.3784	1350.6
298.15	0.4178	1344.5
298.15	0.4620	1337.8
298.15	0.5009	1332.1
298.15	0.5486	1325.3
298.15	0.5814	1320.7
298.15	0.6379	1313.2
298.15	0.6899	1306.4
298.15	0.7389	1299.7
298.15	0.7804	1294.6
298.15	0.8345	1288.1
298.15	0.8929	1281.4
303.15	0.1175	1373.6
303.15	0.1586	1366.3
303.15	0.1952	1359.7
303.15	0.2471	1350.7
303.15	0.2843	1344.4
303.15	0.3396	1335.2
303.15	0.3784	1328.9
303.15	0.4178	1322.6
303.15	0.4620	1315.8
303.15	0.5009	1309.9
303.15	0.5486	1302.9
303.15	0.5814	1298.2
303.15	0.6379	1290.3
303.15	0.6899	1283.4
303.15	0.7389	1277.0
303.15	0.7804	1271.8
303.15	0.8345	1265.3
303.15	0.8929	1258.5
308.15	0.1175	1353.2
308.15	0.1586	1345.6
308.15	0.1952	1339.1
308.15	0.2471	1329.8
308.15	0.2843	1323.4
308.15	0.3396	1314.0
308.15	0.3784	1307.6
308.15	0.4178	1301.2
308.15	0.4620	1294.2
308.15	0.5009	1288.3
308.15	0.5486	1281.1
308.15	0.5814	1276.3
308.15	0.6379	1268.3
308.15	0.6899	1261.3
308.15	0.7389	1254.8
308.15	0.7804	1249.6
308.15	0.8345	1242.9
308.15	0.8929	1236.1

Sources

• Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones