- Name
- 2-Propanol, 2-methyl-
- InChI
- InChI=1S/C4H10O/c1-4(2,3)5/h5H,1-3H3
- InChI Key
- DKGAVHZHDRPRBM-UHFFFAOYSA-N
- Formula
- C4H10O
- SMILES
- CC(C)(C)O
- Mol. Weight (g/mol)
- 74.12
- CAS
- 75-65-0
- Name
- Ethyl formate
- InChI
- InChI=1S/C3H6O2/c1-2-5-3-4/h3H,2H2,1H3
- InChI Key
- WBJINCZRORDGAQ-UHFFFAOYSA-N
- Formula
- C3H6O2
- SMILES
- CCOC=O
- Mol. Weight (g/mol)
- 74.08
- CAS
- 109-94-4
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Datasets
- Mole fraction (2)
- Excess molar enthalpy (molar enthalpy (2)
- Tboil - Boiling temperature at pressure P, K (2)
- Excess molar volume, m3/mol (2)
Mole fraction of Ethyl formate (2) [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Ethyl formate (2) - Liquid | Mole fraction of Ethyl formate (2) - Gas |
|---|---|
| 0.0197 | 0.0712 |
| 0.0380 | 0.1306 |
| 0.0559 | 0.1837 |
| 0.0694 | 0.2210 |
| 0.0989 | 0.2961 |
| 0.1136 | 0.3303 |
| 0.1245 | 0.3530 |
| 0.1528 | 0.4097 |
| 0.1720 | 0.4427 |
| 0.1843 | 0.4626 |
| 0.2037 | 0.4907 |
| 0.2258 | 0.5224 |
| 0.2433 | 0.5452 |
| 0.2637 | 0.5679 |
| 0.2889 | 0.5964 |
| 0.3116 | 0.6194 |
| 0.3409 | 0.6460 |
| 0.3704 | 0.6702 |
| 0.4025 | 0.6939 |
| 0.4314 | 0.7143 |
| 0.4599 | 0.7318 |
| 0.4990 | 0.7555 |
| 0.5095 | 0.7611 |
| 0.5396 | 0.7770 |
| 0.5994 | 0.8066 |
| 0.6664 | 0.8393 |
| 0.6941 | 0.8525 |
| 0.7579 | 0.8842 |
| 0.8025 | 0.9044 |
| 0.8464 | 0.9246 |
| 0.8880 | 0.9443 |
| 0.9216 | 0.9611 |
| 0.9544 | 0.9773 |
| 0.9868 | 0.9933 |
Mole fraction of Ethyl formate (2) [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Ethyl formate (2) - Liquid | Mole fraction of Ethyl formate (2) - Gas |
|---|---|
| 0.0197 | 0.0712 |
| 0.0380 | 0.1306 |
| 0.0559 | 0.1837 |
| 0.0694 | 0.2210 |
| 0.0989 | 0.2961 |
| 0.1136 | 0.3303 |
| 0.1245 | 0.3530 |
| 0.1528 | 0.4097 |
| 0.1720 | 0.4427 |
| 0.1843 | 0.4626 |
| 0.2037 | 0.4907 |
| 0.2258 | 0.5224 |
| 0.2433 | 0.5452 |
| 0.2637 | 0.5679 |
| 0.2889 | 0.5964 |
| 0.3116 | 0.6194 |
| 0.3409 | 0.6460 |
| 0.3704 | 0.6702 |
| 0.4025 | 0.6939 |
| 0.4314 | 0.7143 |
| 0.4599 | 0.7318 |
| 0.4990 | 0.7555 |
| 0.5095 | 0.7611 |
| 0.5396 | 0.7770 |
| 0.5994 | 0.8066 |
| 0.6664 | 0.8393 |
| 0.6941 | 0.8525 |
| 0.7579 | 0.8842 |
| 0.8025 | 0.9044 |
| 0.8464 | 0.9246 |
| 0.8880 | 0.9443 |
| 0.9216 | 0.9611 |
| 0.9544 | 0.9773 |
| 0.9868 | 0.9933 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethyl formate (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 299.15 | 0.0689 | 0.5879 |
| 299.15 | 0.1401 | 1.0647 |
| 299.15 | 0.2146 | 1.4819 |
| 299.15 | 0.2869 | 1.7976 |
| 299.15 | 0.3549 | 1.9993 |
| 299.15 | 0.4172 | 2.1159 |
| 299.15 | 0.4738 | 2.1663 |
| 299.15 | 0.5242 | 2.1639 |
| 299.15 | 0.5696 | 2.1559 |
| 299.15 | 0.5710 | 2.1396 |
| 299.15 | 0.6322 | 2.044 |
| 299.15 | 0.6996 | 1.8688 |
| 299.15 | 0.7701 | 1.6066 |
| 299.15 | 0.8357 | 1.2585 |
| 299.15 | 0.8964 | 0.8928 |
| 299.15 | 0.9485 | 0.4531 |
| 318.15 | 0.0612 | 0.5205 |
| 318.15 | 0.1263 | 0.9163 |
| 318.15 | 0.2016 | 1.3653 |
| 318.15 | 0.2725 | 1.6751 |
| 318.15 | 0.3389 | 1.8549 |
| 318.15 | 0.3986 | 1.9723 |
| 318.15 | 0.4509 | 2.0307 |
| 318.15 | 0.4911 | 2.048 |
| 318.15 | 0.5110 | 2.0516 |
| 318.15 | 0.5304 | 2.0485 |
| 318.15 | 0.5696 | 2.0266 |
| 318.15 | 0.6207 | 1.9869 |
| 318.15 | 0.6806 | 1.8783 |
| 318.15 | 0.7292 | 1.744 |
| 318.15 | 0.7860 | 1.5467 |
| 318.15 | 0.8292 | 1.348 |
| 318.15 | 0.8754 | 1.092 |
| 318.15 | 0.9191 | 0.8054 |
| 318.15 | 0.9757 | 0.3050 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethyl formate (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 299.15 | 0.0689 | 0.5879 |
| 299.15 | 0.1401 | 1.0647 |
| 299.15 | 0.2146 | 1.4819 |
| 299.15 | 0.2869 | 1.7976 |
| 299.15 | 0.3549 | 1.9993 |
| 299.15 | 0.4172 | 2.1159 |
| 299.15 | 0.4738 | 2.1663 |
| 299.15 | 0.5242 | 2.1639 |
| 299.15 | 0.5696 | 2.1559 |
| 299.15 | 0.5710 | 2.1396 |
| 299.15 | 0.6322 | 2.044 |
| 299.15 | 0.6996 | 1.8688 |
| 299.15 | 0.7701 | 1.6066 |
| 299.15 | 0.8357 | 1.2585 |
| 299.15 | 0.8964 | 0.8928 |
| 299.15 | 0.9485 | 0.4531 |
| 318.15 | 0.0612 | 0.5205 |
| 318.15 | 0.1263 | 0.9163 |
| 318.15 | 0.2016 | 1.3653 |
| 318.15 | 0.2725 | 1.6751 |
| 318.15 | 0.3389 | 1.8549 |
| 318.15 | 0.3986 | 1.9723 |
| 318.15 | 0.4509 | 2.0307 |
| 318.15 | 0.4911 | 2.048 |
| 318.15 | 0.5110 | 2.0516 |
| 318.15 | 0.5304 | 2.0485 |
| 318.15 | 0.5696 | 2.0266 |
| 318.15 | 0.6207 | 1.9869 |
| 318.15 | 0.6806 | 1.8783 |
| 318.15 | 0.7292 | 1.744 |
| 318.15 | 0.7860 | 1.5467 |
| 318.15 | 0.8292 | 1.348 |
| 318.15 | 0.8754 | 1.092 |
| 318.15 | 0.9191 | 0.8054 |
| 318.15 | 0.9757 | 0.3050 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Ethyl formate (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0197 | 354.13 |
| 0.0380 | 352.79 |
| 0.0559 | 351.69 |
| 0.0694 | 350.93 |
| 0.0989 | 349.21 |
| 0.1136 | 348.40 |
| 0.1245 | 347.77 |
| 0.1528 | 346.30 |
| 0.1720 | 345.38 |
| 0.1843 | 344.80 |
| 0.2037 | 344.04 |
| 0.2258 | 343.10 |
| 0.2433 | 342.41 |
| 0.2637 | 341.62 |
| 0.2889 | 340.71 |
| 0.3116 | 339.95 |
| 0.3409 | 339.02 |
| 0.3704 | 338.18 |
| 0.4025 | 337.30 |
| 0.4314 | 336.55 |
| 0.4599 | 335.87 |
| 0.4990 | 335.01 |
| 0.5095 | 334.79 |
| 0.5396 | 334.19 |
| 0.5994 | 333.05 |
| 0.6664 | 331.85 |
| 0.6941 | 331.45 |
| 0.7579 | 330.50 |
| 0.8025 | 329.85 |
| 0.8464 | 329.23 |
| 0.8880 | 328.66 |
| 0.9216 | 328.20 |
| 0.9544 | 327.78 |
| 0.9868 | 327.44 |
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Mole fraction of Ethyl formate (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0197 | 354.13 |
| 0.0380 | 352.79 |
| 0.0559 | 351.69 |
| 0.0694 | 350.93 |
| 0.0989 | 349.21 |
| 0.1136 | 348.40 |
| 0.1245 | 347.77 |
| 0.1528 | 346.30 |
| 0.1720 | 345.38 |
| 0.1843 | 344.80 |
| 0.2037 | 344.04 |
| 0.2258 | 343.10 |
| 0.2433 | 342.41 |
| 0.2637 | 341.62 |
| 0.2889 | 340.71 |
| 0.3116 | 339.95 |
| 0.3409 | 339.02 |
| 0.3704 | 338.18 |
| 0.4025 | 337.30 |
| 0.4314 | 336.55 |
| 0.4599 | 335.87 |
| 0.4990 | 335.01 |
| 0.5095 | 334.79 |
| 0.5396 | 334.19 |
| 0.5994 | 333.05 |
| 0.6664 | 331.85 |
| 0.6941 | 331.45 |
| 0.7579 | 330.50 |
| 0.8025 | 329.85 |
| 0.8464 | 329.23 |
| 0.8880 | 328.66 |
| 0.9216 | 328.20 |
| 0.9544 | 327.78 |
| 0.9868 | 327.44 |
Excess molar volume, m3/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethyl formate (2) - Liquid | Excess molar volume, m3/mol - Liquid |
| 303.15 | 0.0451 | 1.6500e-06 |
| 303.15 | 0.0901 | 3.3500e-06 |
| 303.15 | 0.1537 | 5.0600e-06 |
| 303.15 | 0.1973 | 6.0700e-06 |
| 303.15 | 0.2481 | 7.0200e-06 |
| 303.15 | 0.2631 | 7.3200e-06 |
| 303.15 | 0.3042 | 7.9000e-06 |
| 303.15 | 0.3255 | 8.1000e-06 |
| 303.15 | 0.3448 | 8.3000e-06 |
| 303.15 | 0.3957 | 8.6000e-06 |
| 303.15 | 0.4411 | 8.7300e-06 |
| 303.15 | 0.4445 | 8.7500e-06 |
| 303.15 | 0.4964 | 8.7900e-06 |
| 303.15 | 0.5013 | 8.8000e-06 |
| 303.15 | 0.5084 | 8.7800e-06 |
| 303.15 | 0.5344 | 8.7000e-06 |
| 303.15 | 0.5515 | 8.6400e-06 |
| 303.15 | 0.5677 | 8.5800e-06 |
| 303.15 | 0.5954 | 8.3500e-06 |
| 303.15 | 0.6467 | 7.9400e-06 |
| 303.15 | 0.6956 | 7.4200e-06 |
| 303.15 | 0.7432 | 6.5900e-06 |
| 303.15 | 0.8016 | 5.5400e-06 |
| 303.15 | 0.8477 | 4.6300e-06 |
| 303.15 | 0.9067 | 3.2800e-06 |
| 303.15 | 0.9465 | 2.1700e-06 |
| 318.15 | 0.1022 | 4.0900e-06 |
| 318.15 | 0.1289 | 4.8600e-06 |
| 318.15 | 0.2320 | 7.0700e-06 |
| 318.15 | 0.2909 | 7.9600e-06 |
| 318.15 | 0.3356 | 8.4100e-06 |
| 318.15 | 0.4076 | 8.9700e-06 |
| 318.15 | 0.4696 | 9.1700e-06 |
| 318.15 | 0.4934 | 9.1900e-06 |
| 318.15 | 0.5055 | 9.2000e-06 |
| 318.15 | 0.5111 | 9.1900e-06 |
| 318.15 | 0.5267 | 9.1300e-06 |
| 318.15 | 0.5360 | 9.0900e-06 |
| 318.15 | 0.5637 | 8.9100e-06 |
| 318.15 | 0.5859 | 8.7500e-06 |
| 318.15 | 0.6390 | 8.2100e-06 |
| 318.15 | 0.6902 | 7.6000e-06 |
| 318.15 | 0.7388 | 6.8200e-06 |
| 318.15 | 0.7922 | 5.7900e-06 |
| 318.15 | 0.8429 | 4.7100e-06 |
| 318.15 | 0.8913 | 3.4500e-06 |
| 318.15 | 0.9414 | 2.0400e-06 |
Excess molar volume, m3/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethyl formate (2) - Liquid | Excess molar volume, m3/mol - Liquid |
| 303.15 | 0.0451 | 1.6500e-06 |
| 303.15 | 0.0901 | 3.3500e-06 |
| 303.15 | 0.1537 | 5.0600e-06 |
| 303.15 | 0.1973 | 6.0700e-06 |
| 303.15 | 0.2481 | 7.0200e-06 |
| 303.15 | 0.2631 | 7.3200e-06 |
| 303.15 | 0.3042 | 7.9000e-06 |
| 303.15 | 0.3255 | 8.1000e-06 |
| 303.15 | 0.3448 | 8.3000e-06 |
| 303.15 | 0.3957 | 8.6000e-06 |
| 303.15 | 0.4411 | 8.7300e-06 |
| 303.15 | 0.4445 | 8.7500e-06 |
| 303.15 | 0.4964 | 8.7900e-06 |
| 303.15 | 0.5013 | 8.8000e-06 |
| 303.15 | 0.5084 | 8.7800e-06 |
| 303.15 | 0.5344 | 8.7000e-06 |
| 303.15 | 0.5515 | 8.6400e-06 |
| 303.15 | 0.5677 | 8.5800e-06 |
| 303.15 | 0.5954 | 8.3500e-06 |
| 303.15 | 0.6467 | 7.9400e-06 |
| 303.15 | 0.6956 | 7.4200e-06 |
| 303.15 | 0.7432 | 6.5900e-06 |
| 303.15 | 0.8016 | 5.5400e-06 |
| 303.15 | 0.8477 | 4.6300e-06 |
| 303.15 | 0.9067 | 3.2800e-06 |
| 303.15 | 0.9465 | 2.1700e-06 |
| 318.15 | 0.1022 | 4.0900e-06 |
| 318.15 | 0.1289 | 4.8600e-06 |
| 318.15 | 0.2320 | 7.0700e-06 |
| 318.15 | 0.2909 | 7.9600e-06 |
| 318.15 | 0.3356 | 8.4100e-06 |
| 318.15 | 0.4076 | 8.9700e-06 |
| 318.15 | 0.4696 | 9.1700e-06 |
| 318.15 | 0.4934 | 9.1900e-06 |
| 318.15 | 0.5055 | 9.2000e-06 |
| 318.15 | 0.5111 | 9.1900e-06 |
| 318.15 | 0.5267 | 9.1300e-06 |
| 318.15 | 0.5360 | 9.0900e-06 |
| 318.15 | 0.5637 | 8.9100e-06 |
| 318.15 | 0.5859 | 8.7500e-06 |
| 318.15 | 0.6390 | 8.2100e-06 |
| 318.15 | 0.6902 | 7.6000e-06 |
| 318.15 | 0.7388 | 6.8200e-06 |
| 318.15 | 0.7922 | 5.7900e-06 |
| 318.15 | 0.8429 | 4.7100e-06 |
| 318.15 | 0.8913 | 3.4500e-06 |
| 318.15 | 0.9414 | 2.0400e-06 |