Mixture of Tetrahydropyran + Cycloheptanone

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	0.1121	196.30
293.15	0.1652	194.07
293.15	0.2103	192.18
293.15	0.2652	189.86
293.15	0.3187	187.56
293.15	0.3562	185.92
293.15	0.4036	183.78
293.15	0.4562	181.33
293.15	0.4921	179.60
293.15	0.5341	177.51
293.15	0.5896	174.63
293.15	0.6231	172.80
293.15	0.6741	169.93
293.15	0.7256	166.92
293.15	0.7769	163.72
293.15	0.8321	160.14
293.15	0.8754	157.18
293.15	0.9365	152.82
298.15	0.1121	197.43
298.15	0.1652	195.27
298.15	0.2103	193.43
298.15	0.2652	191.15
298.15	0.3187	188.91
298.15	0.3562	187.28
298.15	0.4036	185.22
298.15	0.4562	182.82
298.15	0.4921	181.13
298.15	0.5341	179.07
298.15	0.5896	176.29
298.15	0.6231	174.52
298.15	0.6741	171.69
298.15	0.7256	168.74
298.15	0.7769	165.58
298.15	0.8321	162.00
298.15	0.8754	159.06
298.15	0.9365	154.62
303.15	0.1121	198.93
303.15	0.1652	196.82
303.15	0.2103	195.03
303.15	0.2652	192.76
303.15	0.3187	190.53
303.15	0.3562	188.93
303.15	0.4036	186.84
303.15	0.4562	184.44
303.15	0.4921	182.76
303.15	0.5341	180.74
303.15	0.5896	177.96
303.15	0.6231	176.25
303.15	0.6741	173.45
303.15	0.7256	170.53
303.15	0.7769	167.38
303.15	0.8321	163.83
303.15	0.8754	160.84
303.15	0.9365	156.31
308.15	0.1121	200.52
308.15	0.1652	198.49
308.15	0.2103	196.74
308.15	0.2652	194.53
308.15	0.3187	192.28
308.15	0.3562	190.71
308.15	0.4036	188.65
308.15	0.4562	186.27
308.15	0.4921	184.65
308.15	0.5341	182.63
308.15	0.5896	179.93
308.15	0.6231	178.18
308.15	0.6741	175.49
308.15	0.7256	172.58
308.15	0.7769	169.46
308.15	0.8321	165.92
308.15	0.8754	162.89
308.15	0.9365	158.31

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	0.1121	196.30
293.15	0.1652	194.07
293.15	0.2103	192.18
293.15	0.2652	189.86
293.15	0.3187	187.56
293.15	0.3562	185.92
293.15	0.4036	183.78
293.15	0.4562	181.33
293.15	0.4921	179.60
293.15	0.5341	177.51
293.15	0.5896	174.63
293.15	0.6231	172.80
293.15	0.6741	169.93
293.15	0.7256	166.92
293.15	0.7769	163.72
293.15	0.8321	160.14
293.15	0.8754	157.18
293.15	0.9365	152.82
298.15	0.1121	197.43
298.15	0.1652	195.27
298.15	0.2103	193.43
298.15	0.2652	191.15
298.15	0.3187	188.91
298.15	0.3562	187.28
298.15	0.4036	185.22
298.15	0.4562	182.82
298.15	0.4921	181.13
298.15	0.5341	179.07
298.15	0.5896	176.29
298.15	0.6231	174.52
298.15	0.6741	171.69
298.15	0.7256	168.74
298.15	0.7769	165.58
298.15	0.8321	162.00
298.15	0.8754	159.06
298.15	0.9365	154.62
303.15	0.1121	198.93
303.15	0.1652	196.82
303.15	0.2103	195.03
303.15	0.2652	192.76
303.15	0.3187	190.53
303.15	0.3562	188.93
303.15	0.4036	186.84
303.15	0.4562	184.44
303.15	0.4921	182.76
303.15	0.5341	180.74
303.15	0.5896	177.96
303.15	0.6231	176.25
303.15	0.6741	173.45
303.15	0.7256	170.53
303.15	0.7769	167.38
303.15	0.8321	163.83
303.15	0.8754	160.84
303.15	0.9365	156.31
308.15	0.1121	200.52
308.15	0.1652	198.49
308.15	0.2103	196.74
308.15	0.2652	194.53
308.15	0.3187	192.28
308.15	0.3562	190.71
308.15	0.4036	188.65
308.15	0.4562	186.27
308.15	0.4921	184.65
308.15	0.5341	182.63
308.15	0.5896	179.93
308.15	0.6231	178.18
308.15	0.6741	175.49
308.15	0.7256	172.58
308.15	0.7769	169.46
308.15	0.8321	165.92
308.15	0.8754	162.89
308.15	0.9365	158.31

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

Operational conditions:

• Pressure, kPa = 1e-07 (Liquid)
• Temperature, K = 308.15 (Liquid)

Mole fraction of Tetrahydropyran (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0898	0.0549
0.1356	0.0749
0.1846	0.0896
0.2366	0.1044
0.2882	0.1135
0.3312	0.1188
0.3942	0.1233
0.4412	0.1247
0.4895	0.1245
0.5326	0.1233
0.5842	0.1201
0.6335	0.1160
0.6875	0.1092
0.7289	0.1025
0.7789	0.0920
0.8278	0.0774
0.8799	0.0612
0.9199	0.0434

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

Operational conditions:

• Pressure, kPa = 1e-07 (Liquid)
• Temperature, K = 308.15 (Liquid)

Mole fraction of Tetrahydropyran (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0898	0.0549
0.1356	0.0749
0.1846	0.0896
0.2366	0.1044
0.2882	0.1135
0.3312	0.1188
0.3942	0.1233
0.4412	0.1247
0.4895	0.1245
0.5326	0.1233
0.5842	0.1201
0.6335	0.1160
0.6875	0.1092
0.7289	0.1025
0.7789	0.0920
0.8278	0.0774
0.8799	0.0612
0.9199	0.0434

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	0.0845	948.05
293.15	0.1276	946.02
293.15	0.1794	943.48
293.15	0.2172	941.57
293.15	0.2540	939.66
293.15	0.3098	936.64
293.15	0.3410	934.9
293.15	0.3982	931.59
293.15	0.4407	929.02
293.15	0.4986	925.38
293.15	0.5312	923.24
293.15	0.5779	920.07
293.15	0.6295	916.42
293.15	0.6717	913.29
293.15	0.7229	909.34
293.15	0.7686	905.66
293.15	0.8202	901.28
293.15	0.8742	896.48
298.15	0.0845	943.9
298.15	0.1276	941.88
298.15	0.1794	939.35
298.15	0.2172	937.43
298.15	0.2540	935.51
298.15	0.3098	932.46
298.15	0.3410	930.72
298.15	0.3982	927.36
298.15	0.4407	924.78
298.15	0.4986	921.12
298.15	0.5312	918.96
298.15	0.5779	915.78
298.15	0.6295	912.11
298.15	0.6717	908.95
298.15	0.7229	904.97
298.15	0.7686	901.22
298.15	0.8202	896.77
298.15	0.8742	891.84
303.15	0.0845	939.65
303.15	0.1276	937.63
303.15	0.1794	935.11
303.15	0.2172	933.19
303.15	0.2540	931.26
303.15	0.3098	928.23
303.15	0.3410	926.47
303.15	0.3982	923.12
303.15	0.4407	920.53
303.15	0.4986	916.82
303.15	0.5312	914.66
303.15	0.5779	911.43
303.15	0.6295	907.7
303.15	0.6717	904.49
303.15	0.7229	900.41
303.15	0.7686	896.58
303.15	0.8202	892.03
303.15	0.8742	886.98
308.15	0.0845	935.43
308.15	0.1276	933.42
308.15	0.1794	930.88
308.15	0.2172	928.95
308.15	0.2540	927.02
308.15	0.3098	923.95
308.15	0.3410	922.18
308.15	0.3982	918.8
308.15	0.4407	916.18
308.15	0.4986	912.46
308.15	0.5312	910.27
308.15	0.5779	907.03
308.15	0.6295	903.26
308.15	0.6717	900.02
308.15	0.7229	895.9
308.15	0.7686	892.03
308.15	0.8202	887.39
308.15	0.8742	882.23

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	0.0845	948.05
293.15	0.1276	946.02
293.15	0.1794	943.48
293.15	0.2172	941.57
293.15	0.2540	939.66
293.15	0.3098	936.64
293.15	0.3410	934.9
293.15	0.3982	931.59
293.15	0.4407	929.02
293.15	0.4986	925.38
293.15	0.5312	923.24
293.15	0.5779	920.07
293.15	0.6295	916.42
293.15	0.6717	913.29
293.15	0.7229	909.34
293.15	0.7686	905.66
293.15	0.8202	901.28
293.15	0.8742	896.48
298.15	0.0845	943.9
298.15	0.1276	941.88
298.15	0.1794	939.35
298.15	0.2172	937.43
298.15	0.2540	935.51
298.15	0.3098	932.46
298.15	0.3410	930.72
298.15	0.3982	927.36
298.15	0.4407	924.78
298.15	0.4986	921.12
298.15	0.5312	918.96
298.15	0.5779	915.78
298.15	0.6295	912.11
298.15	0.6717	908.95
298.15	0.7229	904.97
298.15	0.7686	901.22
298.15	0.8202	896.77
298.15	0.8742	891.84
303.15	0.0845	939.65
303.15	0.1276	937.63
303.15	0.1794	935.11
303.15	0.2172	933.19
303.15	0.2540	931.26
303.15	0.3098	928.23
303.15	0.3410	926.47
303.15	0.3982	923.12
303.15	0.4407	920.53
303.15	0.4986	916.82
303.15	0.5312	914.66
303.15	0.5779	911.43
303.15	0.6295	907.7
303.15	0.6717	904.49
303.15	0.7229	900.41
303.15	0.7686	896.58
303.15	0.8202	892.03
303.15	0.8742	886.98
308.15	0.0845	935.43
308.15	0.1276	933.42
308.15	0.1794	930.88
308.15	0.2172	928.95
308.15	0.2540	927.02
308.15	0.3098	923.95
308.15	0.3410	922.18
308.15	0.3982	918.8
308.15	0.4407	916.18
308.15	0.4986	912.46
308.15	0.5312	910.27
308.15	0.5779	907.03
308.15	0.6295	903.26
308.15	0.6717	900.02
308.15	0.7229	895.9
308.15	0.7686	892.03
308.15	0.8202	887.39
308.15	0.8742	882.23

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	0.0845	1457.2
293.15	0.1276	1447.3
293.15	0.1794	1435.5
293.15	0.2172	1427.2
293.15	0.2540	1419.2
293.15	0.3098	1407.4
293.15	0.3410	1400.9
293.15	0.3982	1389.4
293.15	0.4407	1381.2
293.15	0.4986	1370.2
293.15	0.5312	1364.3
293.15	0.5779	1355.9
293.15	0.6295	1347.1
293.15	0.6717	1340.1
293.15	0.7229	1331.9
293.15	0.7686	1324.8
293.15	0.8202	1317.2
293.15	0.8742	1309.5
298.15	0.0845	1435.0
298.15	0.1276	1424.9
298.15	0.1794	1413.0
298.15	0.2172	1404.5
298.15	0.2540	1396.5
298.15	0.3098	1384.5
298.15	0.3410	1378.0
298.15	0.3982	1366.4
298.15	0.4407	1358.0
298.15	0.4986	1346.9
298.15	0.5312	1340.9
298.15	0.5779	1332.6
298.15	0.6295	1323.7
298.15	0.6717	1316.6
298.15	0.7229	1308.4
298.15	0.7686	1301.4
298.15	0.8202	1293.7
298.15	0.8742	1286.1
303.15	0.0845	1411.9
303.15	0.1276	1401.8
303.15	0.1794	1389.8
303.15	0.2172	1381.3
303.15	0.2540	1373.2
303.15	0.3098	1361.1
303.15	0.3410	1354.6
303.15	0.3982	1342.9
303.15	0.4407	1334.6
303.15	0.4986	1323.6
303.15	0.5312	1317.5
303.15	0.5779	1309.2
303.15	0.6295	1300.3
303.15	0.6717	1293.3
303.15	0.7229	1285.2
303.15	0.7686	1278.2
303.15	0.8202	1270.6
303.15	0.8742	1263.0
308.15	0.0845	1389.1
308.15	0.1276	1378.9
308.15	0.1794	1366.9
308.15	0.2172	1358.4
308.15	0.2540	1350.2
308.15	0.3098	1338.2
308.15	0.3410	1331.6
308.15	0.3982	1319.9
308.15	0.4407	1311.6
308.15	0.4986	1300.6
308.15	0.5312	1294.6
308.15	0.5779	1286.3
308.15	0.6295	1277.4
308.15	0.6717	1270.5
308.15	0.7229	1262.4
308.15	0.7686	1255.4
308.15	0.8202	1247.9
308.15	0.8742	1240.4

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	0.0845	1457.2
293.15	0.1276	1447.3
293.15	0.1794	1435.5
293.15	0.2172	1427.2
293.15	0.2540	1419.2
293.15	0.3098	1407.4
293.15	0.3410	1400.9
293.15	0.3982	1389.4
293.15	0.4407	1381.2
293.15	0.4986	1370.2
293.15	0.5312	1364.3
293.15	0.5779	1355.9
293.15	0.6295	1347.1
293.15	0.6717	1340.1
293.15	0.7229	1331.9
293.15	0.7686	1324.8
293.15	0.8202	1317.2
293.15	0.8742	1309.5
298.15	0.0845	1435.0
298.15	0.1276	1424.9
298.15	0.1794	1413.0
298.15	0.2172	1404.5
298.15	0.2540	1396.5
298.15	0.3098	1384.5
298.15	0.3410	1378.0
298.15	0.3982	1366.4
298.15	0.4407	1358.0
298.15	0.4986	1346.9
298.15	0.5312	1340.9
298.15	0.5779	1332.6
298.15	0.6295	1323.7
298.15	0.6717	1316.6
298.15	0.7229	1308.4
298.15	0.7686	1301.4
298.15	0.8202	1293.7
298.15	0.8742	1286.1
303.15	0.0845	1411.9
303.15	0.1276	1401.8
303.15	0.1794	1389.8
303.15	0.2172	1381.3
303.15	0.2540	1373.2
303.15	0.3098	1361.1
303.15	0.3410	1354.6
303.15	0.3982	1342.9
303.15	0.4407	1334.6
303.15	0.4986	1323.6
303.15	0.5312	1317.5
303.15	0.5779	1309.2
303.15	0.6295	1300.3
303.15	0.6717	1293.3
303.15	0.7229	1285.2
303.15	0.7686	1278.2
303.15	0.8202	1270.6
303.15	0.8742	1263.0
308.15	0.0845	1389.1
308.15	0.1276	1378.9
308.15	0.1794	1366.9
308.15	0.2172	1358.4
308.15	0.2540	1350.2
308.15	0.3098	1338.2
308.15	0.3410	1331.6
308.15	0.3982	1319.9
308.15	0.4407	1311.6
308.15	0.4986	1300.6
308.15	0.5312	1294.6
308.15	0.5779	1286.3
308.15	0.6295	1277.4
308.15	0.6717	1270.5
308.15	0.7229	1262.4
308.15	0.7686	1255.4
308.15	0.8202	1247.9
308.15	0.8742	1240.4

Sources

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