- 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
- Name
- Propane, 2-ethoxy-2-methyl-
- InChI
- InChI=1S/C6H14O/c1-5-7-6(2,3)4/h5H2,1-4H3
- InChI Key
- NUMQCACRALPSHD-UHFFFAOYSA-N
- Formula
- C6H14O
- SMILES
- CCOC(C)(C)C
- Mol. Weight (g/mol)
- 102.17
- CAS
- 637-92-3
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Datasets
- Excess molar enthalpy (molar enthalpy (2)
- Pvap - Vapor or sublimation pressure, kPa (4)
- ρl - Mass density, kg/m3 (2)
- csound,fluid - Speed of Sound, m/s (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Temperature, K - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0000 | 298.15 | 0.0000 |
| 0.0000 | 313.15 | 0.0000 |
| 0.0248 | 298.15 | -0.0039 |
| 0.0491 | 298.15 | -0.0073 |
| 0.0499 | 313.15 | -0.0033 |
| 0.0739 | 298.15 | -0.0109 |
| 0.0997 | 313.15 | -0.0054 |
| 0.1003 | 298.15 | -0.0149 |
| 0.1498 | 298.15 | -0.0212 |
| 0.1510 | 313.15 | -0.0093 |
| 0.1991 | 298.15 | -0.0275 |
| 0.2004 | 313.15 | -0.0125 |
| 0.2489 | 298.15 | -0.0324 |
| 0.2511 | 313.15 | -0.0169 |
| 0.2993 | 298.15 | -0.0371 |
| 0.2998 | 313.15 | -0.0200 |
| 0.3499 | 313.15 | -0.0216 |
| 0.3513 | 298.15 | -0.0405 |
| 0.3987 | 298.15 | -0.0433 |
| 0.4011 | 313.15 | -0.0247 |
| 0.4495 | 298.15 | -0.0450 |
| 0.4500 | 313.15 | -0.0254 |
| 0.5003 | 313.15 | -0.0272 |
| 0.5019 | 298.15 | -0.0460 |
| 0.5499 | 313.15 | -0.0265 |
| 0.5515 | 298.15 | -0.0457 |
| 0.5990 | 298.15 | -0.0452 |
| 0.6007 | 313.15 | -0.0250 |
| 0.6491 | 298.15 | -0.0425 |
| 0.6506 | 313.15 | -0.0245 |
| 0.6996 | 313.15 | -0.0229 |
| 0.7014 | 298.15 | -0.0396 |
| 0.7495 | 298.15 | -0.0348 |
| 0.7498 | 313.15 | -0.0206 |
| 0.8010 | 298.15 | -0.0293 |
| 0.8013 | 313.15 | -0.0172 |
| 0.8492 | 313.15 | -0.0143 |
| 0.8514 | 298.15 | -0.0222 |
| 0.9006 | 298.15 | -0.0151 |
| 0.9008 | 313.15 | -0.0100 |
| 0.9510 | 298.15 | -0.0072 |
| 0.9511 | 313.15 | -0.0060 |
| 1.0000 | 298.15 | 0.0000 |
| 1.0000 | 313.15 | 0.0000 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Temperature, K - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0000 | 298.15 | 0.0000 |
| 0.0000 | 313.15 | 0.0000 |
| 0.0248 | 298.15 | -0.0039 |
| 0.0491 | 298.15 | -0.0073 |
| 0.0499 | 313.15 | -0.0033 |
| 0.0739 | 298.15 | -0.0109 |
| 0.0997 | 313.15 | -0.0054 |
| 0.1003 | 298.15 | -0.0149 |
| 0.1498 | 298.15 | -0.0212 |
| 0.1510 | 313.15 | -0.0093 |
| 0.1991 | 298.15 | -0.0275 |
| 0.2004 | 313.15 | -0.0125 |
| 0.2489 | 298.15 | -0.0324 |
| 0.2511 | 313.15 | -0.0169 |
| 0.2993 | 298.15 | -0.0371 |
| 0.2998 | 313.15 | -0.0200 |
| 0.3499 | 313.15 | -0.0216 |
| 0.3513 | 298.15 | -0.0405 |
| 0.3987 | 298.15 | -0.0433 |
| 0.4011 | 313.15 | -0.0247 |
| 0.4495 | 298.15 | -0.0450 |
| 0.4500 | 313.15 | -0.0254 |
| 0.5003 | 313.15 | -0.0272 |
| 0.5019 | 298.15 | -0.0460 |
| 0.5499 | 313.15 | -0.0265 |
| 0.5515 | 298.15 | -0.0457 |
| 0.5990 | 298.15 | -0.0452 |
| 0.6007 | 313.15 | -0.0250 |
| 0.6491 | 298.15 | -0.0425 |
| 0.6506 | 313.15 | -0.0245 |
| 0.6996 | 313.15 | -0.0229 |
| 0.7014 | 298.15 | -0.0396 |
| 0.7495 | 298.15 | -0.0348 |
| 0.7498 | 313.15 | -0.0206 |
| 0.8010 | 298.15 | -0.0293 |
| 0.8013 | 313.15 | -0.0172 |
| 0.8492 | 313.15 | -0.0143 |
| 0.8514 | 298.15 | -0.0222 |
| 0.9006 | 298.15 | -0.0151 |
| 0.9008 | 313.15 | -0.0100 |
| 0.9510 | 298.15 | -0.0072 |
| 0.9511 | 313.15 | -0.0060 |
| 1.0000 | 298.15 | 0.0000 |
| 1.0000 | 313.15 | 0.0000 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.2994 | 15.72 |
| 0.6991 | 24.88 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 7.90 |
| 0.0566 | 9.49 |
| 0.1033 | 10.75 |
| 0.1544 | 12.12 |
| 0.2003 | 13.28 |
| 0.2494 | 14.51 |
| 0.2994 | 15.72 |
| 0.3133 | 16.05 |
| 0.3490 | 16.91 |
| 0.3993 | 18.07 |
| 0.4010 | 18.11 |
| 0.4492 | 19.23 |
| 0.4514 | 19.28 |
| 0.4991 | 20.37 |
| 0.5027 | 20.45 |
| 0.5493 | 21.51 |
| 0.5503 | 21.55 |
| 0.5990 | 22.63 |
| 0.5998 | 22.66 |
| 0.6494 | 23.75 |
| 0.6985 | 24.85 |
| 0.6995 | 24.88 |
| 0.7496 | 25.99 |
| 0.7997 | 27.11 |
| 0.8493 | 28.22 |
| 0.9017 | 29.40 |
| 0.9508 | 30.51 |
| 1.0000 | 31.63 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.2994 | 15.72 |
| 0.6991 | 24.88 |
Vapor or sublimation pressure, kPa [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 7.90 |
| 0.0566 | 9.49 |
| 0.1033 | 10.75 |
| 0.1544 | 12.12 |
| 0.2003 | 13.28 |
| 0.2494 | 14.51 |
| 0.2994 | 15.72 |
| 0.3133 | 16.05 |
| 0.3490 | 16.91 |
| 0.3993 | 18.07 |
| 0.4010 | 18.11 |
| 0.4492 | 19.23 |
| 0.4514 | 19.28 |
| 0.4991 | 20.37 |
| 0.5027 | 20.45 |
| 0.5493 | 21.51 |
| 0.5503 | 21.55 |
| 0.5990 | 22.63 |
| 0.5998 | 22.66 |
| 0.6494 | 23.75 |
| 0.6985 | 24.85 |
| 0.6995 | 24.88 |
| 0.7496 | 25.99 |
| 0.7997 | 27.11 |
| 0.8493 | 28.22 |
| 0.9017 | 29.40 |
| 0.9508 | 30.51 |
| 1.0000 | 31.63 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 871.457 |
| 288.15 | 0.0520 | 864.001 |
| 288.15 | 0.1080 | 855.965 |
| 288.15 | 0.2170 | 840.966 |
| 288.15 | 0.3010 | 829.662 |
| 288.15 | 0.4100 | 815.355 |
| 288.15 | 0.5050 | 803.55 |
| 288.15 | 0.6150 | 789.864 |
| 288.15 | 0.7010 | 779.62 |
| 288.15 | 0.8050 | 767.503 |
| 288.15 | 0.8970 | 757.112 |
| 288.15 | 0.9500 | 751.062 |
| 288.15 | 1.0000 | 745.656 |
| 298.15 | 0.0000 | 862.173 |
| 298.15 | 0.0520 | 854.662 |
| 298.15 | 0.1080 | 846.56 |
| 298.15 | 0.2170 | 831.445 |
| 298.15 | 0.3010 | 820.051 |
| 298.15 | 0.4100 | 805.638 |
| 298.15 | 0.5050 | 793.739 |
| 298.15 | 0.6150 | 779.951 |
| 298.15 | 0.7010 | 769.63 |
| 298.15 | 0.8050 | 757.422 |
| 298.15 | 0.8970 | 746.951 |
| 298.15 | 0.9500 | 740.859 |
| 298.15 | 1.0000 | 735.357 |
| 323.15 | 0.0000 | 838.706 |
| 323.15 | 0.0520 | 831.025 |
| 323.15 | 0.1080 | 822.744 |
| 323.15 | 0.2170 | 807.297 |
| 323.15 | 0.3010 | 795.645 |
| 323.15 | 0.4100 | 780.903 |
| 323.15 | 0.5050 | 768.747 |
| 323.15 | 0.6150 | 754.631 |
| 323.15 | 0.7010 | 744.088 |
| 323.15 | 0.8050 | 731.601 |
| 323.15 | 0.8970 | 720.871 |
| 323.15 | 0.9500 | 714.65 |
| 323.15 | 1.0000 | 709.007 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 871.457 |
| 288.15 | 0.0520 | 864.001 |
| 288.15 | 0.1080 | 855.965 |
| 288.15 | 0.2170 | 840.966 |
| 288.15 | 0.3010 | 829.662 |
| 288.15 | 0.4100 | 815.355 |
| 288.15 | 0.5050 | 803.55 |
| 288.15 | 0.6150 | 789.864 |
| 288.15 | 0.7010 | 779.62 |
| 288.15 | 0.8050 | 767.503 |
| 288.15 | 0.8970 | 757.112 |
| 288.15 | 0.9500 | 751.062 |
| 288.15 | 1.0000 | 745.656 |
| 298.15 | 0.0000 | 862.173 |
| 298.15 | 0.0520 | 854.662 |
| 298.15 | 0.1080 | 846.56 |
| 298.15 | 0.2170 | 831.445 |
| 298.15 | 0.3010 | 820.051 |
| 298.15 | 0.4100 | 805.638 |
| 298.15 | 0.5050 | 793.739 |
| 298.15 | 0.6150 | 779.951 |
| 298.15 | 0.7010 | 769.63 |
| 298.15 | 0.8050 | 757.422 |
| 298.15 | 0.8970 | 746.951 |
| 298.15 | 0.9500 | 740.859 |
| 298.15 | 1.0000 | 735.357 |
| 323.15 | 0.0000 | 838.706 |
| 323.15 | 0.0520 | 831.025 |
| 323.15 | 0.1080 | 822.744 |
| 323.15 | 0.2170 | 807.297 |
| 323.15 | 0.3010 | 795.645 |
| 323.15 | 0.4100 | 780.903 |
| 323.15 | 0.5050 | 768.747 |
| 323.15 | 0.6150 | 754.631 |
| 323.15 | 0.7010 | 744.088 |
| 323.15 | 0.8050 | 731.601 |
| 323.15 | 0.8970 | 720.871 |
| 323.15 | 0.9500 | 714.65 |
| 323.15 | 1.0000 | 709.007 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Speed of sound, m/s - Liquid |
| 288.15 | 0.0000 | 1347.5 |
| 288.15 | 0.0520 | 1332.13 |
| 288.15 | 0.1080 | 1315.25 |
| 288.15 | 0.2170 | 1282.61 |
| 288.15 | 0.3010 | 1258.92 |
| 288.15 | 0.4100 | 1227.96 |
| 288.15 | 0.5050 | 1202.71 |
| 288.15 | 0.6150 | 1173.52 |
| 288.15 | 0.7010 | 1151.45 |
| 288.15 | 0.8050 | 1125.27 |
| 288.15 | 0.8970 | 1102.84 |
| 288.15 | 0.9500 | 1089.79 |
| 288.15 | 1.0000 | 1078.87 |
| 298.15 | 0.0000 | 1303.44 |
| 298.15 | 0.0520 | 1288.26 |
| 298.15 | 0.1080 | 1271.34 |
| 298.15 | 0.2170 | 1238.11 |
| 298.15 | 0.3010 | 1214.71 |
| 298.15 | 0.4100 | 1183.56 |
| 298.15 | 0.5050 | 1158.12 |
| 298.15 | 0.6150 | 1129.12 |
| 298.15 | 0.7010 | 1107.03 |
| 298.15 | 0.8050 | 1080.53 |
| 298.15 | 0.8970 | 1058.16 |
| 298.15 | 0.9500 | 1044.99 |
| 298.15 | 1.0000 | 1033.23 |
| 323.15 | 0.0000 | 1196.6 |
| 323.15 | 0.0520 | 1181.64 |
| 323.15 | 0.1080 | 1163.97 |
| 323.15 | 0.2170 | 1130.58 |
| 323.15 | 0.3010 | 1106.48 |
| 323.15 | 0.4100 | 1074.97 |
| 323.15 | 0.5050 | 1049.33 |
| 323.15 | 0.6150 | 1019.69 |
| 323.15 | 0.7010 | 997.51 |
| 323.15 | 0.8050 | 970.75 |
| 323.15 | 0.8970 | 948.16 |
| 323.15 | 0.9500 | 934.78 |
| 323.15 | 1.0000 | 922.48 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Propane, 2-ethoxy-2-methyl- (2) - Liquid | Speed of sound, m/s - Liquid |
| 288.15 | 0.0000 | 1347.5 |
| 288.15 | 0.0520 | 1332.13 |
| 288.15 | 0.1080 | 1315.25 |
| 288.15 | 0.2170 | 1282.61 |
| 288.15 | 0.3010 | 1258.92 |
| 288.15 | 0.4100 | 1227.96 |
| 288.15 | 0.5050 | 1202.71 |
| 288.15 | 0.6150 | 1173.52 |
| 288.15 | 0.7010 | 1151.45 |
| 288.15 | 0.8050 | 1125.27 |
| 288.15 | 0.8970 | 1102.84 |
| 288.15 | 0.9500 | 1089.79 |
| 288.15 | 1.0000 | 1078.87 |
| 298.15 | 0.0000 | 1303.44 |
| 298.15 | 0.0520 | 1288.26 |
| 298.15 | 0.1080 | 1271.34 |
| 298.15 | 0.2170 | 1238.11 |
| 298.15 | 0.3010 | 1214.71 |
| 298.15 | 0.4100 | 1183.56 |
| 298.15 | 0.5050 | 1158.12 |
| 298.15 | 0.6150 | 1129.12 |
| 298.15 | 0.7010 | 1107.03 |
| 298.15 | 0.8050 | 1080.53 |
| 298.15 | 0.8970 | 1058.16 |
| 298.15 | 0.9500 | 1044.99 |
| 298.15 | 1.0000 | 1033.23 |
| 323.15 | 0.0000 | 1196.6 |
| 323.15 | 0.0520 | 1181.64 |
| 323.15 | 0.1080 | 1163.97 |
| 323.15 | 0.2170 | 1130.58 |
| 323.15 | 0.3010 | 1106.48 |
| 323.15 | 0.4100 | 1074.97 |
| 323.15 | 0.5050 | 1049.33 |
| 323.15 | 0.6150 | 1019.69 |
| 323.15 | 0.7010 | 997.51 |
| 323.15 | 0.8050 | 970.75 |
| 323.15 | 0.8970 | 948.16 |
| 323.15 | 0.9500 | 934.78 |
| 323.15 | 1.0000 | 922.48 |
Sources
- Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
- Thermodynamics of fuels with a bio-synthetic component (IV): (Vapor + liquid) equilibrium data for the ternary mixture (ethyl 1,1-dimethylethyl ether + 1-hexene + toluene) at T = 313.15 K
- Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
- Thermodynamics of Fuels with a Biosynthetic Component: Vapor-Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, n-Heptane, and Toluene at T ) 313.15 K