- 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
- Name
- Isopropyl Alcohol
- InChI
- InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
- InChI Key
- KFZMGEQAYNKOFK-UHFFFAOYSA-N
- Formula
- C3H8O
- SMILES
- CC(C)O
- Mol. Weight (g/mol)
- 60.09
- CAS
- 67-63-0
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Datasets
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethyl formate (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0024 |
| 293.15 | 0.0814 | 0.0018 |
| 293.15 | 0.1589 | 0.0013 |
| 293.15 | 0.2351 | 0.0011 |
| 293.15 | 0.3413 | 0.0008 |
| 293.15 | 0.4351 | 0.0007 |
| 293.15 | 0.5587 | 0.0006 |
| 293.15 | 0.6507 | 0.0005 |
| 293.15 | 0.7349 | 0.0005 |
| 293.15 | 0.8498 | 0.0004 |
| 293.15 | 0.9394 | 0.0004 |
| 293.15 | 1.0000 | 0.0004 |
| 298.15 | 0.0000 | 0.0021 |
| 298.15 | 0.0814 | 0.0015 |
| 298.15 | 0.1589 | 0.0012 |
| 298.15 | 0.2351 | 0.0009 |
| 298.15 | 0.3413 | 0.0008 |
| 298.15 | 0.4351 | 0.0006 |
| 298.15 | 0.5587 | 0.0005 |
| 298.15 | 0.6507 | 0.0005 |
| 298.15 | 0.7349 | 0.0005 |
| 298.15 | 0.8498 | 0.0004 |
| 298.15 | 0.9394 | 0.0004 |
| 298.15 | 1.0000 | 0.0004 |
| 303.15 | 0.0000 | 0.0018 |
| 303.15 | 0.0814 | 0.0014 |
| 303.15 | 0.1589 | 0.0011 |
| 303.15 | 0.2351 | 0.0009 |
| 303.15 | 0.3413 | 0.0007 |
| 303.15 | 0.4351 | 0.0006 |
| 303.15 | 0.5587 | 0.0005 |
| 303.15 | 0.6507 | 0.0005 |
| 303.15 | 0.7349 | 0.0004 |
| 303.15 | 0.8498 | 0.0004 |
| 303.15 | 0.9394 | 0.0004 |
| 303.15 | 1.0000 | 0.0004 |
| 308.15 | 0.0000 | 0.0016 |
| 308.15 | 0.0814 | 0.0012 |
| 308.15 | 0.1589 | 0.0009 |
| 308.15 | 0.2351 | 0.0008 |
| 308.15 | 0.3413 | 0.0006 |
| 308.15 | 0.4351 | 0.0006 |
| 308.15 | 0.5587 | 0.0005 |
| 308.15 | 0.6507 | 0.0004 |
| 308.15 | 0.7349 | 0.0004 |
| 308.15 | 0.8498 | 0.0004 |
| 308.15 | 0.9394 | 0.0004 |
| 308.15 | 1.0000 | 0.0003 |
| 313.15 | 0.0000 | 0.0014 |
| 313.15 | 0.0814 | 0.0010 |
| 313.15 | 0.1589 | 0.0008 |
| 313.15 | 0.2351 | 0.0007 |
| 313.15 | 0.3413 | 0.0006 |
| 313.15 | 0.4351 | 0.0005 |
| 313.15 | 0.5587 | 0.0004 |
| 313.15 | 0.6507 | 0.0004 |
| 313.15 | 0.7349 | 0.0004 |
| 313.15 | 0.8498 | 0.0004 |
| 313.15 | 0.9394 | 0.0003 |
| 313.15 | 1.0000 | 0.0003 |
| 318.15 | 0.0000 | 0.0012 |
| 318.15 | 0.0814 | 0.0009 |
| 318.15 | 0.1589 | 0.0008 |
| 318.15 | 0.2351 | 0.0006 |
| 318.15 | 0.3413 | 0.0005 |
| 318.15 | 0.4351 | 0.0005 |
| 318.15 | 0.5587 | 0.0004 |
| 318.15 | 0.6507 | 0.0004 |
| 318.15 | 0.7349 | 0.0004 |
| 318.15 | 0.8498 | 0.0003 |
| 318.15 | 0.9394 | 0.0003 |
| 318.15 | 1.0000 | 0.0003 |
| 323.15 | 0.0000 | 0.0010 |
| 323.15 | 0.0814 | 0.0008 |
| 323.15 | 0.1589 | 0.0007 |
| 323.15 | 0.2351 | 0.0006 |
| 323.15 | 0.3413 | 0.0005 |
| 323.15 | 0.4351 | 0.0004 |
| 323.15 | 0.5587 | 0.0004 |
| 323.15 | 0.6507 | 0.0004 |
| 323.15 | 0.7349 | 0.0003 |
| 323.15 | 0.8498 | 0.0003 |
| 323.15 | 0.9394 | 0.0003 |
| 323.15 | 1.0000 | 0.0003 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethyl formate (1) - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 0.0000 | 0.0024 |
| 293.15 | 0.0814 | 0.0018 |
| 293.15 | 0.1589 | 0.0013 |
| 293.15 | 0.2351 | 0.0011 |
| 293.15 | 0.3413 | 0.0008 |
| 293.15 | 0.4351 | 0.0007 |
| 293.15 | 0.5587 | 0.0006 |
| 293.15 | 0.6507 | 0.0005 |
| 293.15 | 0.7349 | 0.0005 |
| 293.15 | 0.8498 | 0.0004 |
| 293.15 | 0.9394 | 0.0004 |
| 293.15 | 1.0000 | 0.0004 |
| 298.15 | 0.0000 | 0.0021 |
| 298.15 | 0.0814 | 0.0015 |
| 298.15 | 0.1589 | 0.0012 |
| 298.15 | 0.2351 | 0.0009 |
| 298.15 | 0.3413 | 0.0008 |
| 298.15 | 0.4351 | 0.0006 |
| 298.15 | 0.5587 | 0.0005 |
| 298.15 | 0.6507 | 0.0005 |
| 298.15 | 0.7349 | 0.0005 |
| 298.15 | 0.8498 | 0.0004 |
| 298.15 | 0.9394 | 0.0004 |
| 298.15 | 1.0000 | 0.0004 |
| 303.15 | 0.0000 | 0.0018 |
| 303.15 | 0.0814 | 0.0014 |
| 303.15 | 0.1589 | 0.0011 |
| 303.15 | 0.2351 | 0.0009 |
| 303.15 | 0.3413 | 0.0007 |
| 303.15 | 0.4351 | 0.0006 |
| 303.15 | 0.5587 | 0.0005 |
| 303.15 | 0.6507 | 0.0005 |
| 303.15 | 0.7349 | 0.0004 |
| 303.15 | 0.8498 | 0.0004 |
| 303.15 | 0.9394 | 0.0004 |
| 303.15 | 1.0000 | 0.0004 |
| 308.15 | 0.0000 | 0.0016 |
| 308.15 | 0.0814 | 0.0012 |
| 308.15 | 0.1589 | 0.0009 |
| 308.15 | 0.2351 | 0.0008 |
| 308.15 | 0.3413 | 0.0006 |
| 308.15 | 0.4351 | 0.0006 |
| 308.15 | 0.5587 | 0.0005 |
| 308.15 | 0.6507 | 0.0004 |
| 308.15 | 0.7349 | 0.0004 |
| 308.15 | 0.8498 | 0.0004 |
| 308.15 | 0.9394 | 0.0004 |
| 308.15 | 1.0000 | 0.0003 |
| 313.15 | 0.0000 | 0.0014 |
| 313.15 | 0.0814 | 0.0010 |
| 313.15 | 0.1589 | 0.0008 |
| 313.15 | 0.2351 | 0.0007 |
| 313.15 | 0.3413 | 0.0006 |
| 313.15 | 0.4351 | 0.0005 |
| 313.15 | 0.5587 | 0.0004 |
| 313.15 | 0.6507 | 0.0004 |
| 313.15 | 0.7349 | 0.0004 |
| 313.15 | 0.8498 | 0.0004 |
| 313.15 | 0.9394 | 0.0003 |
| 313.15 | 1.0000 | 0.0003 |
| 318.15 | 0.0000 | 0.0012 |
| 318.15 | 0.0814 | 0.0009 |
| 318.15 | 0.1589 | 0.0008 |
| 318.15 | 0.2351 | 0.0006 |
| 318.15 | 0.3413 | 0.0005 |
| 318.15 | 0.4351 | 0.0005 |
| 318.15 | 0.5587 | 0.0004 |
| 318.15 | 0.6507 | 0.0004 |
| 318.15 | 0.7349 | 0.0004 |
| 318.15 | 0.8498 | 0.0003 |
| 318.15 | 0.9394 | 0.0003 |
| 318.15 | 1.0000 | 0.0003 |
| 323.15 | 0.0000 | 0.0010 |
| 323.15 | 0.0814 | 0.0008 |
| 323.15 | 0.1589 | 0.0007 |
| 323.15 | 0.2351 | 0.0006 |
| 323.15 | 0.3413 | 0.0005 |
| 323.15 | 0.4351 | 0.0004 |
| 323.15 | 0.5587 | 0.0004 |
| 323.15 | 0.6507 | 0.0004 |
| 323.15 | 0.7349 | 0.0003 |
| 323.15 | 0.8498 | 0.0003 |
| 323.15 | 0.9394 | 0.0003 |
| 323.15 | 1.0000 | 0.0003 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Ethyl formate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 5000.00 | 0.0498 | 0.3371 |
| 298.15 | 5000.00 | 0.0993 | 0.6619 |
| 298.15 | 5000.00 | 0.1485 | 0.9260 |
| 298.15 | 5000.00 | 0.2008 | 1.1529 |
| 298.15 | 5000.00 | 0.2493 | 1.3245 |
| 298.15 | 5000.00 | 0.3009 | 1.4641 |
| 298.15 | 5000.00 | 0.3488 | 1.5616 |
| 298.15 | 5000.00 | 0.3997 | 1.635 |
| 298.15 | 5000.00 | 0.4503 | 1.675 |
| 298.15 | 5000.00 | 0.5005 | 1.6869 |
| 298.15 | 5000.00 | 0.5504 | 1.6652 |
| 298.15 | 5000.00 | 0.5999 | 1.6276 |
| 298.15 | 5000.00 | 0.6492 | 1.5569 |
| 298.15 | 5000.00 | 0.7013 | 1.4374 |
| 298.15 | 5000.00 | 0.7498 | 1.2999 |
| 298.15 | 5000.00 | 0.8012 | 1.1171 |
| 298.15 | 5000.00 | 0.8997 | 0.6544 |
| 298.15 | 5000.00 | 0.9500 | 0.3587 |
| 298.15 | 10000.00 | 0.0497 | 0.3099 |
| 298.15 | 10000.00 | 0.0990 | 0.6379 |
| 298.15 | 10000.00 | 0.1516 | 0.9142 |
| 298.15 | 10000.00 | 0.2003 | 1.1323 |
| 298.15 | 10000.00 | 0.2487 | 1.3015 |
| 298.15 | 10000.00 | 0.3002 | 1.4435 |
| 298.15 | 10000.00 | 0.3514 | 1.5392 |
| 298.15 | 10000.00 | 0.3989 | 1.6029 |
| 298.15 | 10000.00 | 0.4495 | 1.644 |
| 298.15 | 10000.00 | 0.4997 | 1.6555 |
| 298.15 | 10000.00 | 0.5496 | 1.6437 |
| 298.15 | 10000.00 | 0.5991 | 1.6055 |
| 298.15 | 10000.00 | 0.6484 | 1.5379 |
| 298.15 | 10000.00 | 0.7006 | 1.4234 |
| 298.15 | 10000.00 | 0.7492 | 1.2986 |
| 298.15 | 10000.00 | 0.8006 | 1.1083 |
| 298.15 | 10000.00 | 0.8994 | 0.6550 |
| 298.15 | 10000.00 | 0.9499 | 0.3617 |
| 308.15 | 10000.00 | 0.0487 | 0.2137 |
| 308.15 | 10000.00 | 0.1000 | 0.5803 |
| 308.15 | 10000.00 | 0.1511 | 0.8840 |
| 308.15 | 10000.00 | 0.1988 | 1.116 |
| 308.15 | 10000.00 | 0.2492 | 1.3115 |
| 308.15 | 10000.00 | 0.2993 | 1.4676 |
| 308.15 | 10000.00 | 0.3490 | 1.5829 |
| 308.15 | 10000.00 | 0.4013 | 1.6663 |
| 308.15 | 10000.00 | 0.4504 | 1.7131 |
| 308.15 | 10000.00 | 0.4992 | 1.7276 |
| 308.15 | 10000.00 | 0.5505 | 1.7125 |
| 308.15 | 10000.00 | 0.5987 | 1.6704 |
| 308.15 | 10000.00 | 0.6996 | 1.476 |
| 308.15 | 10000.00 | 0.7496 | 1.3361 |
| 308.15 | 10000.00 | 0.7993 | 1.1638 |
| 308.15 | 10000.00 | 0.8513 | 0.9437 |
| 308.15 | 10000.00 | 0.9003 | 0.6831 |
| 308.15 | 10000.00 | 0.9490 | 0.3811 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
| Fixed | Measured | ||
|---|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mole fraction of Ethyl formate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 298.15 | 5000.00 | 0.0498 | 0.3371 |
| 298.15 | 5000.00 | 0.0993 | 0.6619 |
| 298.15 | 5000.00 | 0.1485 | 0.9260 |
| 298.15 | 5000.00 | 0.2008 | 1.1529 |
| 298.15 | 5000.00 | 0.2493 | 1.3245 |
| 298.15 | 5000.00 | 0.3009 | 1.4641 |
| 298.15 | 5000.00 | 0.3488 | 1.5616 |
| 298.15 | 5000.00 | 0.3997 | 1.635 |
| 298.15 | 5000.00 | 0.4503 | 1.675 |
| 298.15 | 5000.00 | 0.5005 | 1.6869 |
| 298.15 | 5000.00 | 0.5504 | 1.6652 |
| 298.15 | 5000.00 | 0.5999 | 1.6276 |
| 298.15 | 5000.00 | 0.6492 | 1.5569 |
| 298.15 | 5000.00 | 0.7013 | 1.4374 |
| 298.15 | 5000.00 | 0.7498 | 1.2999 |
| 298.15 | 5000.00 | 0.8012 | 1.1171 |
| 298.15 | 5000.00 | 0.8997 | 0.6544 |
| 298.15 | 5000.00 | 0.9500 | 0.3587 |
| 298.15 | 10000.00 | 0.0497 | 0.3099 |
| 298.15 | 10000.00 | 0.0990 | 0.6379 |
| 298.15 | 10000.00 | 0.1516 | 0.9142 |
| 298.15 | 10000.00 | 0.2003 | 1.1323 |
| 298.15 | 10000.00 | 0.2487 | 1.3015 |
| 298.15 | 10000.00 | 0.3002 | 1.4435 |
| 298.15 | 10000.00 | 0.3514 | 1.5392 |
| 298.15 | 10000.00 | 0.3989 | 1.6029 |
| 298.15 | 10000.00 | 0.4495 | 1.644 |
| 298.15 | 10000.00 | 0.4997 | 1.6555 |
| 298.15 | 10000.00 | 0.5496 | 1.6437 |
| 298.15 | 10000.00 | 0.5991 | 1.6055 |
| 298.15 | 10000.00 | 0.6484 | 1.5379 |
| 298.15 | 10000.00 | 0.7006 | 1.4234 |
| 298.15 | 10000.00 | 0.7492 | 1.2986 |
| 298.15 | 10000.00 | 0.8006 | 1.1083 |
| 298.15 | 10000.00 | 0.8994 | 0.6550 |
| 298.15 | 10000.00 | 0.9499 | 0.3617 |
| 308.15 | 10000.00 | 0.0487 | 0.2137 |
| 308.15 | 10000.00 | 0.1000 | 0.5803 |
| 308.15 | 10000.00 | 0.1511 | 0.8840 |
| 308.15 | 10000.00 | 0.1988 | 1.116 |
| 308.15 | 10000.00 | 0.2492 | 1.3115 |
| 308.15 | 10000.00 | 0.2993 | 1.4676 |
| 308.15 | 10000.00 | 0.3490 | 1.5829 |
| 308.15 | 10000.00 | 0.4013 | 1.6663 |
| 308.15 | 10000.00 | 0.4504 | 1.7131 |
| 308.15 | 10000.00 | 0.4992 | 1.7276 |
| 308.15 | 10000.00 | 0.5505 | 1.7125 |
| 308.15 | 10000.00 | 0.5987 | 1.6704 |
| 308.15 | 10000.00 | 0.6996 | 1.476 |
| 308.15 | 10000.00 | 0.7496 | 1.3361 |
| 308.15 | 10000.00 | 0.7993 | 1.1638 |
| 308.15 | 10000.00 | 0.8513 | 0.9437 |
| 308.15 | 10000.00 | 0.9003 | 0.6831 |
| 308.15 | 10000.00 | 0.9490 | 0.3811 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethyl formate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 785.4 |
| 293.15 | 0.0814 | 795.4 |
| 293.15 | 0.1589 | 804.8 |
| 293.15 | 0.2351 | 814.0 |
| 293.15 | 0.3413 | 826.8 |
| 293.15 | 0.4351 | 838.3 |
| 293.15 | 0.5587 | 853.9 |
| 293.15 | 0.6507 | 865.7 |
| 293.15 | 0.7349 | 877.1 |
| 293.15 | 0.8498 | 893.5 |
| 293.15 | 0.9394 | 907.1 |
| 293.15 | 1.0000 | 916.6 |
| 298.15 | 0.0000 | 781.1 |
| 298.15 | 0.0814 | 790.7 |
| 298.15 | 0.1589 | 799.9 |
| 298.15 | 0.2351 | 808.8 |
| 298.15 | 0.3413 | 821.5 |
| 298.15 | 0.4351 | 832.8 |
| 298.15 | 0.5587 | 848.2 |
| 298.15 | 0.6507 | 859.9 |
| 298.15 | 0.7349 | 871.0 |
| 298.15 | 0.8498 | 887.2 |
| 298.15 | 0.9394 | 900.6 |
| 298.15 | 1.0000 | 910.1 |
| 303.15 | 0.0000 | 776.8 |
| 303.15 | 0.0814 | 786.1 |
| 303.15 | 0.1589 | 795.0 |
| 303.15 | 0.2351 | 803.8 |
| 303.15 | 0.3413 | 816.2 |
| 303.15 | 0.4351 | 827.4 |
| 303.15 | 0.5587 | 842.5 |
| 303.15 | 0.6507 | 854.0 |
| 303.15 | 0.7349 | 865.0 |
| 303.15 | 0.8498 | 880.8 |
| 303.15 | 0.9394 | 894.0 |
| 303.15 | 1.0000 | 903.6 |
| 308.15 | 0.0000 | 772.4 |
| 308.15 | 0.0814 | 781.4 |
| 308.15 | 0.1589 | 790.1 |
| 308.15 | 0.2351 | 798.8 |
| 308.15 | 0.3413 | 811.0 |
| 308.15 | 0.4351 | 822.0 |
| 308.15 | 0.5587 | 836.8 |
| 308.15 | 0.6507 | 848.0 |
| 308.15 | 0.7349 | 858.6 |
| 308.15 | 0.8498 | 874.1 |
| 308.15 | 0.9394 | 887.3 |
| 308.15 | 1.0000 | 897.1 |
| 313.15 | 0.0000 | 768.0 |
| 313.15 | 0.0814 | 776.6 |
| 313.15 | 0.1589 | 785.1 |
| 313.15 | 0.2351 | 793.6 |
| 313.15 | 0.3413 | 805.7 |
| 313.15 | 0.4351 | 816.5 |
| 313.15 | 0.5587 | 831.1 |
| 313.15 | 0.6507 | 842.1 |
| 313.15 | 0.7349 | 852.4 |
| 313.15 | 0.8498 | 867.6 |
| 313.15 | 0.9394 | 880.8 |
| 313.15 | 1.0000 | 890.5 |
| 318.15 | 0.0000 | 763.4 |
| 318.15 | 0.0814 | 771.8 |
| 318.15 | 0.1589 | 780.1 |
| 318.15 | 0.2351 | 788.3 |
| 318.15 | 0.3413 | 800.0 |
| 318.15 | 0.4351 | 810.5 |
| 318.15 | 0.5587 | 824.7 |
| 318.15 | 0.6507 | 835.4 |
| 318.15 | 0.7349 | 845.6 |
| 318.15 | 0.8498 | 860.4 |
| 318.15 | 0.9394 | 873.5 |
| 318.15 | 1.0000 | 883.0 |
| 323.15 | 0.0000 | 758.8 |
| 323.15 | 0.0814 | 766.7 |
| 323.15 | 0.1589 | 774.8 |
| 323.15 | 0.2351 | 782.8 |
| 323.15 | 0.3413 | 794.4 |
| 323.15 | 0.4351 | 804.8 |
| 323.15 | 0.5587 | 818.6 |
| 323.15 | 0.6507 | 829.2 |
| 323.15 | 0.7349 | 839.1 |
| 323.15 | 0.8498 | 853.8 |
| 323.15 | 0.9394 | 866.7 |
| 323.15 | 1.0000 | 876.0 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 100 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethyl formate (1) - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 0.0000 | 785.4 |
| 293.15 | 0.0814 | 795.4 |
| 293.15 | 0.1589 | 804.8 |
| 293.15 | 0.2351 | 814.0 |
| 293.15 | 0.3413 | 826.8 |
| 293.15 | 0.4351 | 838.3 |
| 293.15 | 0.5587 | 853.9 |
| 293.15 | 0.6507 | 865.7 |
| 293.15 | 0.7349 | 877.1 |
| 293.15 | 0.8498 | 893.5 |
| 293.15 | 0.9394 | 907.1 |
| 293.15 | 1.0000 | 916.6 |
| 298.15 | 0.0000 | 781.1 |
| 298.15 | 0.0814 | 790.7 |
| 298.15 | 0.1589 | 799.9 |
| 298.15 | 0.2351 | 808.8 |
| 298.15 | 0.3413 | 821.5 |
| 298.15 | 0.4351 | 832.8 |
| 298.15 | 0.5587 | 848.2 |
| 298.15 | 0.6507 | 859.9 |
| 298.15 | 0.7349 | 871.0 |
| 298.15 | 0.8498 | 887.2 |
| 298.15 | 0.9394 | 900.6 |
| 298.15 | 1.0000 | 910.1 |
| 303.15 | 0.0000 | 776.8 |
| 303.15 | 0.0814 | 786.1 |
| 303.15 | 0.1589 | 795.0 |
| 303.15 | 0.2351 | 803.8 |
| 303.15 | 0.3413 | 816.2 |
| 303.15 | 0.4351 | 827.4 |
| 303.15 | 0.5587 | 842.5 |
| 303.15 | 0.6507 | 854.0 |
| 303.15 | 0.7349 | 865.0 |
| 303.15 | 0.8498 | 880.8 |
| 303.15 | 0.9394 | 894.0 |
| 303.15 | 1.0000 | 903.6 |
| 308.15 | 0.0000 | 772.4 |
| 308.15 | 0.0814 | 781.4 |
| 308.15 | 0.1589 | 790.1 |
| 308.15 | 0.2351 | 798.8 |
| 308.15 | 0.3413 | 811.0 |
| 308.15 | 0.4351 | 822.0 |
| 308.15 | 0.5587 | 836.8 |
| 308.15 | 0.6507 | 848.0 |
| 308.15 | 0.7349 | 858.6 |
| 308.15 | 0.8498 | 874.1 |
| 308.15 | 0.9394 | 887.3 |
| 308.15 | 1.0000 | 897.1 |
| 313.15 | 0.0000 | 768.0 |
| 313.15 | 0.0814 | 776.6 |
| 313.15 | 0.1589 | 785.1 |
| 313.15 | 0.2351 | 793.6 |
| 313.15 | 0.3413 | 805.7 |
| 313.15 | 0.4351 | 816.5 |
| 313.15 | 0.5587 | 831.1 |
| 313.15 | 0.6507 | 842.1 |
| 313.15 | 0.7349 | 852.4 |
| 313.15 | 0.8498 | 867.6 |
| 313.15 | 0.9394 | 880.8 |
| 313.15 | 1.0000 | 890.5 |
| 318.15 | 0.0000 | 763.4 |
| 318.15 | 0.0814 | 771.8 |
| 318.15 | 0.1589 | 780.1 |
| 318.15 | 0.2351 | 788.3 |
| 318.15 | 0.3413 | 800.0 |
| 318.15 | 0.4351 | 810.5 |
| 318.15 | 0.5587 | 824.7 |
| 318.15 | 0.6507 | 835.4 |
| 318.15 | 0.7349 | 845.6 |
| 318.15 | 0.8498 | 860.4 |
| 318.15 | 0.9394 | 873.5 |
| 318.15 | 1.0000 | 883.0 |
| 323.15 | 0.0000 | 758.8 |
| 323.15 | 0.0814 | 766.7 |
| 323.15 | 0.1589 | 774.8 |
| 323.15 | 0.2351 | 782.8 |
| 323.15 | 0.3413 | 794.4 |
| 323.15 | 0.4351 | 804.8 |
| 323.15 | 0.5587 | 818.6 |
| 323.15 | 0.6507 | 829.2 |
| 323.15 | 0.7349 | 839.1 |
| 323.15 | 0.8498 | 853.8 |
| 323.15 | 0.9394 | 866.7 |
| 323.15 | 1.0000 | 876.0 |