- Name
- Propane, 2-methoxy-2-methyl-
- InChI
- InChI=1S/C5H12O/c1-5(2,3)6-4/h1-4H3
- InChI Key
- BZLVMXJERCGZMT-UHFFFAOYSA-N
- Formula
- C5H12O
- SMILES
- COC(C)(C)C
- Mol. Weight (g/mol)
- 88.15
- CAS
- 1634-04-4
- Name
- Nonane
- InChI
- InChI=1S/C9H20/c1-3-5-7-9-8-6-4-2/h3-9H2,1-2H3
- InChI Key
- BKIMMITUMNQMOS-UHFFFAOYSA-N
- Formula
- C9H20
- SMILES
- CCCCCCCCC
- Mol. Weight (g/mol)
- 128.26
- CAS
- 111-84-2
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Datasets
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 273.15 | 0.0000 | 0.0010 |
| 273.15 | 0.1006 | 0.0009 |
| 273.15 | 0.2026 | 0.0008 |
| 273.15 | 0.2995 | 0.0008 |
| 273.15 | 0.4045 | 0.0007 |
| 273.15 | 0.5003 | 0.0007 |
| 273.15 | 0.6035 | 0.0006 |
| 273.15 | 0.6998 | 0.0006 |
| 273.15 | 0.7975 | 0.0005 |
| 273.15 | 0.8971 | 0.0005 |
| 278.15 | 0.0000 | 0.0009 |
| 278.15 | 0.1006 | 0.0008 |
| 278.15 | 0.2026 | 0.0008 |
| 278.15 | 0.2995 | 0.0007 |
| 278.15 | 0.4045 | 0.0007 |
| 278.15 | 0.5003 | 0.0006 |
| 278.15 | 0.6035 | 0.0006 |
| 278.15 | 0.6998 | 0.0005 |
| 278.15 | 0.7975 | 0.0005 |
| 278.15 | 0.8971 | 0.0005 |
| 283.15 | 0.0000 | 0.0008 |
| 283.15 | 0.1006 | 0.0008 |
| 283.15 | 0.2026 | 0.0007 |
| 283.15 | 0.2995 | 0.0007 |
| 283.15 | 0.4045 | 0.0006 |
| 283.15 | 0.5003 | 0.0006 |
| 283.15 | 0.6035 | 0.0006 |
| 283.15 | 0.6998 | 0.0005 |
| 283.15 | 0.7975 | 0.0005 |
| 283.15 | 0.8971 | 0.0004 |
| 288.15 | 0.0000 | 0.0008 |
| 288.15 | 0.1006 | 0.0007 |
| 288.15 | 0.2026 | 0.0007 |
| 288.15 | 0.2995 | 0.0006 |
| 288.15 | 0.4045 | 0.0006 |
| 288.15 | 0.5003 | 0.0006 |
| 288.15 | 0.6035 | 0.0005 |
| 288.15 | 0.6998 | 0.0005 |
| 288.15 | 0.7975 | 0.0004 |
| 288.15 | 0.8971 | 0.0004 |
| 293.15 | 0.0000 | 0.0007 |
| 293.15 | 0.1006 | 0.0007 |
| 293.15 | 0.2026 | 0.0006 |
| 293.15 | 0.2995 | 0.0006 |
| 293.15 | 0.4045 | 0.0006 |
| 293.15 | 0.5003 | 0.0005 |
| 293.15 | 0.6035 | 0.0005 |
| 293.15 | 0.6998 | 0.0005 |
| 293.15 | 0.7975 | 0.0004 |
| 293.15 | 0.8971 | 0.0004 |
| 298.15 | 0.0000 | 0.0007 |
| 298.15 | 0.1006 | 0.0006 |
| 298.15 | 0.2026 | 0.0006 |
| 298.15 | 0.2995 | 0.0006 |
| 298.15 | 0.4045 | 0.0005 |
| 298.15 | 0.5003 | 0.0005 |
| 298.15 | 0.6035 | 0.0005 |
| 298.15 | 0.6998 | 0.0004 |
| 298.15 | 0.7975 | 0.0004 |
| 298.15 | 0.8971 | 0.0004 |
| 303.15 | 0.0000 | 0.0006 |
| 303.15 | 0.1006 | 0.0006 |
| 303.15 | 0.2026 | 0.0006 |
| 303.15 | 0.2995 | 0.0005 |
| 303.15 | 0.4045 | 0.0005 |
| 303.15 | 0.5003 | 0.0005 |
| 303.15 | 0.6035 | 0.0004 |
| 303.15 | 0.6998 | 0.0004 |
| 303.15 | 0.7975 | 0.0004 |
| 308.15 | 0.0000 | 0.0006 |
| 308.15 | 0.1006 | 0.0006 |
| 308.15 | 0.2026 | 0.0005 |
| 308.15 | 0.2995 | 0.0005 |
| 308.15 | 0.4045 | 0.0005 |
| 308.15 | 0.5003 | 0.0004 |
| 308.15 | 0.6035 | 0.0004 |
| 308.15 | 0.6998 | 0.0004 |
| 308.15 | 0.7975 | 0.0004 |
| 313.15 | 0.0000 | 0.0006 |
| 313.15 | 0.1006 | 0.0005 |
| 313.15 | 0.2026 | 0.0005 |
| 313.15 | 0.2995 | 0.0005 |
| 313.15 | 0.4045 | 0.0004 |
| 313.15 | 0.5003 | 0.0004 |
| 313.15 | 0.6035 | 0.0004 |
| 313.15 | 0.6998 | 0.0004 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.1006 | 0.0005 |
| 318.15 | 0.2026 | 0.0005 |
| 318.15 | 0.2995 | 0.0004 |
| 318.15 | 0.4045 | 0.0004 |
| 318.15 | 0.5003 | 0.0004 |
| 318.15 | 0.6035 | 0.0004 |
| 318.15 | 0.6998 | 0.0003 |
| 323.15 | 0.0000 | 0.0005 |
| 323.15 | 0.1006 | 0.0005 |
| 323.15 | 0.2026 | 0.0004 |
| 323.15 | 0.2995 | 0.0004 |
| 323.15 | 0.4045 | 0.0004 |
| 323.15 | 0.5003 | 0.0004 |
| 323.15 | 0.6035 | 0.0004 |
| 328.15 | 0.0000 | 0.0005 |
| 328.15 | 0.1006 | 0.0004 |
| 328.15 | 0.2026 | 0.0004 |
| 328.15 | 0.2995 | 0.0004 |
| 328.15 | 0.4045 | 0.0004 |
| 328.15 | 0.5003 | 0.0004 |
| 333.15 | 0.0000 | 0.0004 |
| 333.15 | 0.1006 | 0.0004 |
| 333.15 | 0.2026 | 0.0004 |
| 333.15 | 0.2995 | 0.0004 |
| 333.15 | 0.4045 | 0.0004 |
| 333.15 | 0.5003 | 0.0003 |
| 338.15 | 0.0000 | 0.0004 |
| 338.15 | 0.1006 | 0.0004 |
| 338.15 | 0.2026 | 0.0004 |
| 338.15 | 0.2995 | 0.0004 |
| 338.15 | 0.4045 | 0.0003 |
| 343.15 | 0.0000 | 0.0004 |
| 343.15 | 0.1006 | 0.0004 |
| 343.15 | 0.2026 | 0.0004 |
| 343.15 | 0.2995 | 0.0004 |
| 348.15 | 0.0000 | 0.0004 |
| 348.15 | 0.1006 | 0.0004 |
| 348.15 | 0.2026 | 0.0004 |
| 353.15 | 0.0000 | 0.0004 |
| 353.15 | 0.1006 | 0.0003 |
| 353.15 | 0.2026 | 0.0003 |
| 358.15 | 0.0000 | 0.0003 |
| 358.15 | 0.1006 | 0.0003 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 273.15 | 0.0000 | 0.0010 |
| 273.15 | 0.1006 | 0.0009 |
| 273.15 | 0.2026 | 0.0008 |
| 273.15 | 0.2995 | 0.0008 |
| 273.15 | 0.4045 | 0.0007 |
| 273.15 | 0.5003 | 0.0007 |
| 273.15 | 0.6035 | 0.0006 |
| 273.15 | 0.6998 | 0.0006 |
| 273.15 | 0.7975 | 0.0005 |
| 273.15 | 0.8971 | 0.0005 |
| 278.15 | 0.0000 | 0.0009 |
| 278.15 | 0.1006 | 0.0008 |
| 278.15 | 0.2026 | 0.0008 |
| 278.15 | 0.2995 | 0.0007 |
| 278.15 | 0.4045 | 0.0007 |
| 278.15 | 0.5003 | 0.0006 |
| 278.15 | 0.6035 | 0.0006 |
| 278.15 | 0.6998 | 0.0005 |
| 278.15 | 0.7975 | 0.0005 |
| 278.15 | 0.8971 | 0.0005 |
| 283.15 | 0.0000 | 0.0008 |
| 283.15 | 0.1006 | 0.0008 |
| 283.15 | 0.2026 | 0.0007 |
| 283.15 | 0.2995 | 0.0007 |
| 283.15 | 0.4045 | 0.0006 |
| 283.15 | 0.5003 | 0.0006 |
| 283.15 | 0.6035 | 0.0006 |
| 283.15 | 0.6998 | 0.0005 |
| 283.15 | 0.7975 | 0.0005 |
| 283.15 | 0.8971 | 0.0004 |
| 288.15 | 0.0000 | 0.0008 |
| 288.15 | 0.1006 | 0.0007 |
| 288.15 | 0.2026 | 0.0007 |
| 288.15 | 0.2995 | 0.0006 |
| 288.15 | 0.4045 | 0.0006 |
| 288.15 | 0.5003 | 0.0006 |
| 288.15 | 0.6035 | 0.0005 |
| 288.15 | 0.6998 | 0.0005 |
| 288.15 | 0.7975 | 0.0004 |
| 288.15 | 0.8971 | 0.0004 |
| 293.15 | 0.0000 | 0.0007 |
| 293.15 | 0.1006 | 0.0007 |
| 293.15 | 0.2026 | 0.0006 |
| 293.15 | 0.2995 | 0.0006 |
| 293.15 | 0.4045 | 0.0006 |
| 293.15 | 0.5003 | 0.0005 |
| 293.15 | 0.6035 | 0.0005 |
| 293.15 | 0.6998 | 0.0005 |
| 293.15 | 0.7975 | 0.0004 |
| 293.15 | 0.8971 | 0.0004 |
| 298.15 | 0.0000 | 0.0007 |
| 298.15 | 0.1006 | 0.0006 |
| 298.15 | 0.2026 | 0.0006 |
| 298.15 | 0.2995 | 0.0006 |
| 298.15 | 0.4045 | 0.0005 |
| 298.15 | 0.5003 | 0.0005 |
| 298.15 | 0.6035 | 0.0005 |
| 298.15 | 0.6998 | 0.0004 |
| 298.15 | 0.7975 | 0.0004 |
| 298.15 | 0.8971 | 0.0004 |
| 303.15 | 0.0000 | 0.0006 |
| 303.15 | 0.1006 | 0.0006 |
| 303.15 | 0.2026 | 0.0006 |
| 303.15 | 0.2995 | 0.0005 |
| 303.15 | 0.4045 | 0.0005 |
| 303.15 | 0.5003 | 0.0005 |
| 303.15 | 0.6035 | 0.0004 |
| 303.15 | 0.6998 | 0.0004 |
| 303.15 | 0.7975 | 0.0004 |
| 308.15 | 0.0000 | 0.0006 |
| 308.15 | 0.1006 | 0.0006 |
| 308.15 | 0.2026 | 0.0005 |
| 308.15 | 0.2995 | 0.0005 |
| 308.15 | 0.4045 | 0.0005 |
| 308.15 | 0.5003 | 0.0004 |
| 308.15 | 0.6035 | 0.0004 |
| 308.15 | 0.6998 | 0.0004 |
| 308.15 | 0.7975 | 0.0004 |
| 313.15 | 0.0000 | 0.0006 |
| 313.15 | 0.1006 | 0.0005 |
| 313.15 | 0.2026 | 0.0005 |
| 313.15 | 0.2995 | 0.0005 |
| 313.15 | 0.4045 | 0.0004 |
| 313.15 | 0.5003 | 0.0004 |
| 313.15 | 0.6035 | 0.0004 |
| 313.15 | 0.6998 | 0.0004 |
| 318.15 | 0.0000 | 0.0005 |
| 318.15 | 0.1006 | 0.0005 |
| 318.15 | 0.2026 | 0.0005 |
| 318.15 | 0.2995 | 0.0004 |
| 318.15 | 0.4045 | 0.0004 |
| 318.15 | 0.5003 | 0.0004 |
| 318.15 | 0.6035 | 0.0004 |
| 318.15 | 0.6998 | 0.0003 |
| 323.15 | 0.0000 | 0.0005 |
| 323.15 | 0.1006 | 0.0005 |
| 323.15 | 0.2026 | 0.0004 |
| 323.15 | 0.2995 | 0.0004 |
| 323.15 | 0.4045 | 0.0004 |
| 323.15 | 0.5003 | 0.0004 |
| 323.15 | 0.6035 | 0.0004 |
| 328.15 | 0.0000 | 0.0005 |
| 328.15 | 0.1006 | 0.0004 |
| 328.15 | 0.2026 | 0.0004 |
| 328.15 | 0.2995 | 0.0004 |
| 328.15 | 0.4045 | 0.0004 |
| 328.15 | 0.5003 | 0.0004 |
| 333.15 | 0.0000 | 0.0004 |
| 333.15 | 0.1006 | 0.0004 |
| 333.15 | 0.2026 | 0.0004 |
| 333.15 | 0.2995 | 0.0004 |
| 333.15 | 0.4045 | 0.0004 |
| 333.15 | 0.5003 | 0.0003 |
| 338.15 | 0.0000 | 0.0004 |
| 338.15 | 0.1006 | 0.0004 |
| 338.15 | 0.2026 | 0.0004 |
| 338.15 | 0.2995 | 0.0004 |
| 338.15 | 0.4045 | 0.0003 |
| 343.15 | 0.0000 | 0.0004 |
| 343.15 | 0.1006 | 0.0004 |
| 343.15 | 0.2026 | 0.0004 |
| 343.15 | 0.2995 | 0.0004 |
| 348.15 | 0.0000 | 0.0004 |
| 348.15 | 0.1006 | 0.0004 |
| 348.15 | 0.2026 | 0.0004 |
| 353.15 | 0.0000 | 0.0004 |
| 353.15 | 0.1006 | 0.0003 |
| 353.15 | 0.2026 | 0.0003 |
| 358.15 | 0.0000 | 0.0003 |
| 358.15 | 0.1006 | 0.0003 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0816 | 0.1310 |
| 0.1472 | 0.2250 |
| 0.1747 | 0.2650 |
| 0.2383 | 0.3450 |
| 0.2404 | 0.3450 |
| 0.3312 | 0.4280 |
| 0.3912 | 0.4570 |
| 0.4867 | 0.4860 |
| 0.6601 | 0.4370 |
| 0.7157 | 0.3920 |
| 0.7399 | 0.3710 |
| 0.7773 | 0.3370 |
| 0.8129 | 0.3050 |
| 0.8723 | 0.2310 |
| 0.8950 | 0.2000 |
| 0.9235 | 0.1730 |
| 0.9285 | 0.1410 |
| 0.9459 | 0.1260 |
| 0.9573 | 0.1040 |
| 0.9632 | 0.0820 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0816 | 0.1310 |
| 0.1472 | 0.2250 |
| 0.1747 | 0.2650 |
| 0.2383 | 0.3450 |
| 0.2404 | 0.3450 |
| 0.3312 | 0.4280 |
| 0.3912 | 0.4570 |
| 0.4867 | 0.4860 |
| 0.6601 | 0.4370 |
| 0.7157 | 0.3920 |
| 0.7399 | 0.3710 |
| 0.7773 | 0.3370 |
| 0.8129 | 0.3050 |
| 0.8723 | 0.2310 |
| 0.8950 | 0.2000 |
| 0.9235 | 0.1730 |
| 0.9285 | 0.1410 |
| 0.9459 | 0.1260 |
| 0.9573 | 0.1040 |
| 0.9632 | 0.0820 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 273.15 | 0.0000 | 733.184 |
| 273.15 | 0.1085 | 734.69 |
| 273.15 | 0.1722 | 735.67 |
| 273.15 | 0.3037 | 737.89 |
| 273.15 | 0.4011 | 739.94 |
| 273.15 | 0.5008 | 742.31 |
| 273.15 | 0.6005 | 745.08 |
| 273.15 | 0.6992 | 748.17 |
| 273.15 | 0.8005 | 751.89 |
| 273.15 | 0.8925 | 755.81 |
| 273.15 | 1.0000 | 761.34 |
| 278.15 | 0.0000 | 729.335 |
| 278.15 | 0.1085 | 730.78 |
| 278.15 | 0.1722 | 731.71 |
| 278.15 | 0.3037 | 733.82 |
| 278.15 | 0.4011 | 735.78 |
| 278.15 | 0.5008 | 738.04 |
| 278.15 | 0.6005 | 740.68 |
| 278.15 | 0.6992 | 743.64 |
| 278.15 | 0.8005 | 747.2 |
| 278.15 | 0.8925 | 750.95 |
| 278.15 | 1.0000 | 756.14 |
| 283.15 | 0.0000 | 725.473 |
| 283.15 | 0.1085 | 726.84 |
| 283.15 | 0.1722 | 727.73 |
| 283.15 | 0.3037 | 729.73 |
| 283.15 | 0.4011 | 731.59 |
| 283.15 | 0.5008 | 733.74 |
| 283.15 | 0.6005 | 736.26 |
| 283.15 | 0.6992 | 739.08 |
| 283.15 | 0.8005 | 742.47 |
| 283.15 | 0.8925 | 746.06 |
| 283.15 | 1.0000 | 751.02 |
| 288.15 | 0.0000 | 721.603 |
| 288.15 | 0.1085 | 722.9 |
| 288.15 | 0.1722 | 723.73 |
| 288.15 | 0.3037 | 725.62 |
| 288.15 | 0.4011 | 727.39 |
| 288.15 | 0.5008 | 729.43 |
| 288.15 | 0.6005 | 731.81 |
| 288.15 | 0.6992 | 734.49 |
| 288.15 | 0.8005 | 737.72 |
| 288.15 | 0.8925 | 741.13 |
| 288.15 | 1.0000 | 745.85 |
| 293.15 | 0.0000 | 717.725 |
| 293.15 | 0.1085 | 718.92 |
| 293.15 | 0.1722 | 719.72 |
| 293.15 | 0.3037 | 721.51 |
| 293.15 | 0.4011 | 723.16 |
| 293.15 | 0.5008 | 725.09 |
| 293.15 | 0.6005 | 727.34 |
| 293.15 | 0.6992 | 729.87 |
| 293.15 | 0.8005 | 732.94 |
| 293.15 | 0.8925 | 736.17 |
| 293.15 | 1.0000 | 740.65 |
| 298.15 | 0.0000 | 713.834 |
| 298.15 | 0.1085 | 714.95 |
| 298.15 | 0.1722 | 715.7 |
| 298.15 | 0.3037 | 717.36 |
| 298.15 | 0.4011 | 718.92 |
| 298.15 | 0.5008 | 720.73 |
| 298.15 | 0.6005 | 722.84 |
| 298.15 | 0.6992 | 725.22 |
| 298.15 | 0.8005 | 728.11 |
| 298.15 | 0.8925 | 731.18 |
| 298.15 | 1.0000 | 735.4 |
| 303.15 | 0.0000 | 709.929 |
| 303.15 | 0.1085 | 710.96 |
| 303.15 | 0.1722 | 711.66 |
| 303.15 | 0.3037 | 713.21 |
| 303.15 | 0.4011 | 714.65 |
| 303.15 | 0.5008 | 716.34 |
| 303.15 | 0.6005 | 718.32 |
| 303.15 | 0.6992 | 720.55 |
| 303.15 | 0.8005 | 723.25 |
| 303.15 | 0.8925 | 726.13 |
| 303.15 | 1.0000 | 730.1 |
| 308.15 | 0.0000 | 706.011 |
| 308.15 | 0.1085 | 706.97 |
| 308.15 | 0.1722 | 707.6 |
| 308.15 | 0.3037 | 709.03 |
| 308.15 | 0.4011 | 710.36 |
| 308.15 | 0.5008 | 711.93 |
| 308.15 | 0.6005 | 713.77 |
| 308.15 | 0.6992 | 715.84 |
| 308.15 | 0.8005 | 718.35 |
| 308.15 | 0.8925 | 721.04 |
| 308.15 | 1.0000 | 724.82 |
| 313.15 | 0.0000 | 702.076 |
| 313.15 | 0.1085 | 702.96 |
| 313.15 | 0.1722 | 703.52 |
| 313.15 | 0.3037 | 704.82 |
| 313.15 | 0.4011 | 706.05 |
| 313.15 | 0.5008 | 707.49 |
| 313.15 | 0.6005 | 709.18 |
| 313.15 | 0.6992 | 711.09 |
| 313.15 | 0.8005 | 713.41 |
| 313.15 | 0.8925 | 715.91 |
| 313.15 | 1.0000 | 719.42 |
| 318.15 | 0.0000 | 698.124 |
| 318.15 | 0.1085 | 698.89 |
| 318.15 | 0.1722 | 699.42 |
| 318.15 | 0.3037 | 700.6 |
| 318.15 | 0.4011 | 701.71 |
| 318.15 | 0.5008 | 703.01 |
| 318.15 | 0.6005 | 704.56 |
| 318.15 | 0.6992 | 706.3 |
| 318.15 | 0.8005 | 708.45 |
| 318.15 | 0.8925 | 710.72 |
| 318.15 | 1.0000 | 713.96 |
| 323.15 | 0.0000 | 694.151 |
| 323.15 | 0.1085 | 694.83 |
| 323.15 | 0.1722 | 695.3 |
| 323.15 | 0.3037 | 696.34 |
| 323.15 | 0.4011 | 697.34 |
| 323.15 | 0.5008 | 698.51 |
| 323.15 | 0.6005 | 699.89 |
| 323.15 | 0.6992 | 701.46 |
| 323.15 | 0.8005 | 703.35 |
| 323.15 | 0.8925 | 705.48 |
| 328.15 | 0.0000 | 690.165 |
| 328.15 | 0.1085 | 690.74 |
| 328.15 | 0.1722 | 691.16 |
| 328.15 | 0.3037 | 692.06 |
| 328.15 | 0.4011 | 692.94 |
| 328.15 | 0.5008 | 693.97 |
| 328.15 | 0.6005 | 695.19 |
| 328.15 | 0.6992 | 696.59 |
| 328.15 | 0.8005 | 698.27 |
| 333.15 | 0.0000 | 686.154 |
| 333.15 | 0.1085 | 686.64 |
| 333.15 | 0.1722 | 686.99 |
| 333.15 | 0.3037 | 687.76 |
| 333.15 | 0.4011 | 688.5 |
| 333.15 | 0.5008 | 689.39 |
| 333.15 | 0.6005 | 690.45 |
| 333.15 | 0.6992 | 691.66 |
| 333.15 | 0.8005 | 693.14 |
| 338.15 | 0.0000 | 682.116 |
| 338.15 | 0.1085 | 682.52 |
| 338.15 | 0.1722 | 682.79 |
| 338.15 | 0.3037 | 683.42 |
| 338.15 | 0.4011 | 684.02 |
| 338.15 | 0.5008 | 684.76 |
| 338.15 | 0.6005 | 685.66 |
| 338.15 | 0.6992 | 686.68 |
| 338.15 | 0.8005 | 687.95 |
| 343.15 | 0.0000 | 678.06 |
| 343.15 | 0.1085 | 678.37 |
| 343.15 | 0.1722 | 678.57 |
| 343.15 | 0.3037 | 679.05 |
| 343.15 | 0.4011 | 679.52 |
| 343.15 | 0.5008 | 680.11 |
| 343.15 | 0.6005 | 680.83 |
| 348.15 | 0.0000 | 673.979 |
| 348.15 | 0.1085 | 674.19 |
| 348.15 | 0.1722 | 674.31 |
| 348.15 | 0.3037 | 674.64 |
| 348.15 | 0.4011 | 674.98 |
| 353.15 | 0.0000 | 669.872 |
| 353.15 | 0.1085 | 669.95 |
| 353.15 | 0.1722 | 670.02 |
| 353.15 | 0.3037 | 670.19 |
| 353.15 | 0.4011 | 670.38 |
| 358.15 | 0.0000 | 665.73 |
| 358.15 | 0.1085 | 665.71 |
| 358.15 | 0.1722 | 665.7 |
| 358.15 | 0.3037 | 665.7 |
| 358.15 | 0.4011 | 665.75 |
| 363.15 | 0.0000 | 661.557 |
| 363.16 | 0.1085 | 661.43 |
| 363.16 | 0.1722 | 661.33 |
| 363.16 | 0.3037 | 661.17 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 273.15 | 0.0000 | 733.184 |
| 273.15 | 0.1085 | 734.69 |
| 273.15 | 0.1722 | 735.67 |
| 273.15 | 0.3037 | 737.89 |
| 273.15 | 0.4011 | 739.94 |
| 273.15 | 0.5008 | 742.31 |
| 273.15 | 0.6005 | 745.08 |
| 273.15 | 0.6992 | 748.17 |
| 273.15 | 0.8005 | 751.89 |
| 273.15 | 0.8925 | 755.81 |
| 273.15 | 1.0000 | 761.34 |
| 278.15 | 0.0000 | 729.335 |
| 278.15 | 0.1085 | 730.78 |
| 278.15 | 0.1722 | 731.71 |
| 278.15 | 0.3037 | 733.82 |
| 278.15 | 0.4011 | 735.78 |
| 278.15 | 0.5008 | 738.04 |
| 278.15 | 0.6005 | 740.68 |
| 278.15 | 0.6992 | 743.64 |
| 278.15 | 0.8005 | 747.2 |
| 278.15 | 0.8925 | 750.95 |
| 278.15 | 1.0000 | 756.14 |
| 283.15 | 0.0000 | 725.473 |
| 283.15 | 0.1085 | 726.84 |
| 283.15 | 0.1722 | 727.73 |
| 283.15 | 0.3037 | 729.73 |
| 283.15 | 0.4011 | 731.59 |
| 283.15 | 0.5008 | 733.74 |
| 283.15 | 0.6005 | 736.26 |
| 283.15 | 0.6992 | 739.08 |
| 283.15 | 0.8005 | 742.47 |
| 283.15 | 0.8925 | 746.06 |
| 283.15 | 1.0000 | 751.02 |
| 288.15 | 0.0000 | 721.603 |
| 288.15 | 0.1085 | 722.9 |
| 288.15 | 0.1722 | 723.73 |
| 288.15 | 0.3037 | 725.62 |
| 288.15 | 0.4011 | 727.39 |
| 288.15 | 0.5008 | 729.43 |
| 288.15 | 0.6005 | 731.81 |
| 288.15 | 0.6992 | 734.49 |
| 288.15 | 0.8005 | 737.72 |
| 288.15 | 0.8925 | 741.13 |
| 288.15 | 1.0000 | 745.85 |
| 293.15 | 0.0000 | 717.725 |
| 293.15 | 0.1085 | 718.92 |
| 293.15 | 0.1722 | 719.72 |
| 293.15 | 0.3037 | 721.51 |
| 293.15 | 0.4011 | 723.16 |
| 293.15 | 0.5008 | 725.09 |
| 293.15 | 0.6005 | 727.34 |
| 293.15 | 0.6992 | 729.87 |
| 293.15 | 0.8005 | 732.94 |
| 293.15 | 0.8925 | 736.17 |
| 293.15 | 1.0000 | 740.65 |
| 298.15 | 0.0000 | 713.834 |
| 298.15 | 0.1085 | 714.95 |
| 298.15 | 0.1722 | 715.7 |
| 298.15 | 0.3037 | 717.36 |
| 298.15 | 0.4011 | 718.92 |
| 298.15 | 0.5008 | 720.73 |
| 298.15 | 0.6005 | 722.84 |
| 298.15 | 0.6992 | 725.22 |
| 298.15 | 0.8005 | 728.11 |
| 298.15 | 0.8925 | 731.18 |
| 298.15 | 1.0000 | 735.4 |
| 303.15 | 0.0000 | 709.929 |
| 303.15 | 0.1085 | 710.96 |
| 303.15 | 0.1722 | 711.66 |
| 303.15 | 0.3037 | 713.21 |
| 303.15 | 0.4011 | 714.65 |
| 303.15 | 0.5008 | 716.34 |
| 303.15 | 0.6005 | 718.32 |
| 303.15 | 0.6992 | 720.55 |
| 303.15 | 0.8005 | 723.25 |
| 303.15 | 0.8925 | 726.13 |
| 303.15 | 1.0000 | 730.1 |
| 308.15 | 0.0000 | 706.011 |
| 308.15 | 0.1085 | 706.97 |
| 308.15 | 0.1722 | 707.6 |
| 308.15 | 0.3037 | 709.03 |
| 308.15 | 0.4011 | 710.36 |
| 308.15 | 0.5008 | 711.93 |
| 308.15 | 0.6005 | 713.77 |
| 308.15 | 0.6992 | 715.84 |
| 308.15 | 0.8005 | 718.35 |
| 308.15 | 0.8925 | 721.04 |
| 308.15 | 1.0000 | 724.82 |
| 313.15 | 0.0000 | 702.076 |
| 313.15 | 0.1085 | 702.96 |
| 313.15 | 0.1722 | 703.52 |
| 313.15 | 0.3037 | 704.82 |
| 313.15 | 0.4011 | 706.05 |
| 313.15 | 0.5008 | 707.49 |
| 313.15 | 0.6005 | 709.18 |
| 313.15 | 0.6992 | 711.09 |
| 313.15 | 0.8005 | 713.41 |
| 313.15 | 0.8925 | 715.91 |
| 313.15 | 1.0000 | 719.42 |
| 318.15 | 0.0000 | 698.124 |
| 318.15 | 0.1085 | 698.89 |
| 318.15 | 0.1722 | 699.42 |
| 318.15 | 0.3037 | 700.6 |
| 318.15 | 0.4011 | 701.71 |
| 318.15 | 0.5008 | 703.01 |
| 318.15 | 0.6005 | 704.56 |
| 318.15 | 0.6992 | 706.3 |
| 318.15 | 0.8005 | 708.45 |
| 318.15 | 0.8925 | 710.72 |
| 318.15 | 1.0000 | 713.96 |
| 323.15 | 0.0000 | 694.151 |
| 323.15 | 0.1085 | 694.83 |
| 323.15 | 0.1722 | 695.3 |
| 323.15 | 0.3037 | 696.34 |
| 323.15 | 0.4011 | 697.34 |
| 323.15 | 0.5008 | 698.51 |
| 323.15 | 0.6005 | 699.89 |
| 323.15 | 0.6992 | 701.46 |
| 323.15 | 0.8005 | 703.35 |
| 323.15 | 0.8925 | 705.48 |
| 328.15 | 0.0000 | 690.165 |
| 328.15 | 0.1085 | 690.74 |
| 328.15 | 0.1722 | 691.16 |
| 328.15 | 0.3037 | 692.06 |
| 328.15 | 0.4011 | 692.94 |
| 328.15 | 0.5008 | 693.97 |
| 328.15 | 0.6005 | 695.19 |
| 328.15 | 0.6992 | 696.59 |
| 328.15 | 0.8005 | 698.27 |
| 333.15 | 0.0000 | 686.154 |
| 333.15 | 0.1085 | 686.64 |
| 333.15 | 0.1722 | 686.99 |
| 333.15 | 0.3037 | 687.76 |
| 333.15 | 0.4011 | 688.5 |
| 333.15 | 0.5008 | 689.39 |
| 333.15 | 0.6005 | 690.45 |
| 333.15 | 0.6992 | 691.66 |
| 333.15 | 0.8005 | 693.14 |
| 338.15 | 0.0000 | 682.116 |
| 338.15 | 0.1085 | 682.52 |
| 338.15 | 0.1722 | 682.79 |
| 338.15 | 0.3037 | 683.42 |
| 338.15 | 0.4011 | 684.02 |
| 338.15 | 0.5008 | 684.76 |
| 338.15 | 0.6005 | 685.66 |
| 338.15 | 0.6992 | 686.68 |
| 338.15 | 0.8005 | 687.95 |
| 343.15 | 0.0000 | 678.06 |
| 343.15 | 0.1085 | 678.37 |
| 343.15 | 0.1722 | 678.57 |
| 343.15 | 0.3037 | 679.05 |
| 343.15 | 0.4011 | 679.52 |
| 343.15 | 0.5008 | 680.11 |
| 343.15 | 0.6005 | 680.83 |
| 348.15 | 0.0000 | 673.979 |
| 348.15 | 0.1085 | 674.19 |
| 348.15 | 0.1722 | 674.31 |
| 348.15 | 0.3037 | 674.64 |
| 348.15 | 0.4011 | 674.98 |
| 353.15 | 0.0000 | 669.872 |
| 353.15 | 0.1085 | 669.95 |
| 353.15 | 0.1722 | 670.02 |
| 353.15 | 0.3037 | 670.19 |
| 353.15 | 0.4011 | 670.38 |
| 358.15 | 0.0000 | 665.73 |
| 358.15 | 0.1085 | 665.71 |
| 358.15 | 0.1722 | 665.7 |
| 358.15 | 0.3037 | 665.7 |
| 358.15 | 0.4011 | 665.75 |
| 363.15 | 0.0000 | 661.557 |
| 363.16 | 0.1085 | 661.43 |
| 363.16 | 0.1722 | 661.33 |
| 363.16 | 0.3037 | 661.17 |
Sources
- Determination of excess molar enthalpies of the ternary system methyl tert-butyl ether + 1-pentanol + nonane at 298.15K Analysis and comparison with predicted values of the UNIFAC model and some empirical methods
- Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K