- Name
- Propene
- InChI
- InChI=1S/C3H6/c1-3-2/h3H,1H2,2H3
- InChI Key
- QQONPFPTGQHPMA-UHFFFAOYSA-N
- Formula
- C3H6
- SMILES
- C=CC
- Mol. Weight (g/mol)
- 42.08
- CAS
- 115-07-1
- 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
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Datasets
Mole fraction of Isopropyl Alcohol (2) [ref]
Operational condition: Temperature, K = 313.15 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 | Mole fraction of Isopropyl Alcohol (2) - Liquid mixture 1 |
|---|---|
| 1381.00 | 0.1188 |
| 1403.00 | 0.1136 |
| 1424.00 | 0.1031 |
| 1473.00 | 0.0971 |
| 1488.00 | 0.0894 |
| 1516.00 | 0.0801 |
| 1590.00 | 0.0534 |
| 1690.00 | 0.0000 |
Mole fraction of Isopropyl Alcohol (2) [ref]
Operational condition: Temperature, K = 313.15 (Liquid mixture 2)
| Pressure, kPa - Liquid mixture 2 | Mole fraction of Isopropyl Alcohol (2) - Liquid mixture 2 |
|---|---|
| 1381.00 | 0.3678 |
| 1403.00 | 0.3876 |
| 1424.00 | 0.3952 |
| 1473.00 | 0.4040 |
| 1488.00 | 0.4054 |
| 1516.00 | 0.3990 |
| 1590.00 | 0.1628 |
| 1690.00 | 0.0000 |
Mole fraction of Isopropyl Alcohol (2) [ref]
Operational condition: Temperature, K = 313.15 (Gas)
| Pressure, kPa - Gas | Mole fraction of Isopropyl Alcohol (2) - Gas |
|---|---|
| 1424.00 | 0.0089 |
| 1488.00 | 0.0083 |
| 1516.00 | 0.0085 |
| 1590.00 | 0.0069 |
Mole fraction of Propene (1) [ref]
Operational condition: Temperature, K = 313.15 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 | Mole fraction of Propene (1) - Liquid mixture 1 |
|---|---|
| 1381.00 | 0.0097 |
| 1403.00 | 0.0080 |
| 1424.00 | 0.0063 |
| 1473.00 | 0.0046 |
| 1488.00 | 0.0041 |
| 1516.00 | 0.0034 |
| 1590.00 | 0.0019 |
| 1690.00 | 0.0008 |
Mole fraction of Propene (1) [ref]
Operational condition: Temperature, K = 313.15 (Liquid mixture 2)
| Pressure, kPa - Liquid mixture 2 | Mole fraction of Propene (1) - Liquid mixture 2 |
|---|---|
| 1381.00 | 0.1437 |
| 1403.00 | 0.1710 |
| 1424.00 | 0.2048 |
| 1473.00 | 0.2836 |
| 1488.00 | 0.3079 |
| 1516.00 | 0.3846 |
| 1590.00 | 0.8047 |
| 1690.00 | 0.9917 |
Mole fraction of Propene (1) [ref]
Operational condition: Temperature, K = 313.15 (Gas)
| Pressure, kPa - Gas | Mole fraction of Propene (1) - Gas |
|---|---|
| 1424.00 | 0.9825 |
| 1488.00 | 0.9838 |
| 1516.00 | 0.9915 |
| 1590.00 | 0.9850 |
Mole fraction of Isopropyl Alcohol (2) [ref]
Operational condition: Temperature, K = 313.15 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 | Mole fraction of Isopropyl Alcohol (2) - Liquid mixture 1 |
|---|---|
| 1381.00 | 0.1188 |
| 1403.00 | 0.1136 |
| 1424.00 | 0.1031 |
| 1473.00 | 0.0971 |
| 1488.00 | 0.0894 |
| 1516.00 | 0.0801 |
| 1590.00 | 0.0534 |
| 1690.00 | 0.0000 |
Mole fraction of Isopropyl Alcohol (2) [ref]
Operational condition: Temperature, K = 313.15 (Liquid mixture 2)
| Pressure, kPa - Liquid mixture 2 | Mole fraction of Isopropyl Alcohol (2) - Liquid mixture 2 |
|---|---|
| 1381.00 | 0.3678 |
| 1403.00 | 0.3876 |
| 1424.00 | 0.3952 |
| 1473.00 | 0.4040 |
| 1488.00 | 0.4054 |
| 1516.00 | 0.3990 |
| 1590.00 | 0.1628 |
| 1690.00 | 0.0000 |
Mole fraction of Isopropyl Alcohol (2) [ref]
Operational condition: Temperature, K = 313.15 (Gas)
| Pressure, kPa - Gas | Mole fraction of Isopropyl Alcohol (2) - Gas |
|---|---|
| 1424.00 | 0.0089 |
| 1488.00 | 0.0083 |
| 1516.00 | 0.0085 |
| 1590.00 | 0.0069 |
Mole fraction of Propene (1) [ref]
Operational condition: Temperature, K = 313.15 (Liquid mixture 1)
| Pressure, kPa - Liquid mixture 1 | Mole fraction of Propene (1) - Liquid mixture 1 |
|---|---|
| 1381.00 | 0.0097 |
| 1403.00 | 0.0080 |
| 1424.00 | 0.0063 |
| 1473.00 | 0.0046 |
| 1488.00 | 0.0041 |
| 1516.00 | 0.0034 |
| 1590.00 | 0.0019 |
| 1690.00 | 0.0008 |
Mole fraction of Propene (1) [ref]
Operational condition: Temperature, K = 313.15 (Liquid mixture 2)
| Pressure, kPa - Liquid mixture 2 | Mole fraction of Propene (1) - Liquid mixture 2 |
|---|---|
| 1381.00 | 0.1437 |
| 1403.00 | 0.1710 |
| 1424.00 | 0.2048 |
| 1473.00 | 0.2836 |
| 1488.00 | 0.3079 |
| 1516.00 | 0.3846 |
| 1590.00 | 0.8047 |
| 1690.00 | 0.9917 |
Mole fraction of Propene (1) [ref]
Operational condition: Temperature, K = 313.15 (Gas)
| Pressure, kPa - Gas | Mole fraction of Propene (1) - Gas |
|---|---|
| 1424.00 | 0.9825 |
| 1488.00 | 0.9838 |
| 1516.00 | 0.9915 |
| 1590.00 | 0.9850 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Pressure, kPa - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Water (3) - Liquid | Mole fraction of Propene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 1997.00 | 1.0121 | 0.0503 | 0.1317 |
| 1997.00 | 1.0121 | 0.1006 | 0.2347 |
| 1997.00 | 1.0121 | 0.1508 | 0.3104 |
| 1997.00 | 1.0121 | 0.2010 | 0.3651 |
| 1997.00 | 1.0121 | 0.2512 | 0.4043 |
| 1997.00 | 1.0121 | 0.3013 | 0.4298 |
| 1997.00 | 1.0121 | 0.4015 | 0.4707 |
| 1997.00 | 1.0121 | 0.5016 | 0.5018 |
| 1997.00 | 1.0121 | 0.6015 | 0.5248 |
| 1997.00 | 1.0121 | 0.6514 | 0.5298 |
| 1997.00 | 1.0121 | 0.7013 | 0.5316 |
| 1997.00 | 1.0121 | 0.8010 | 0.5147 |
| 1997.00 | 1.0121 | 0.9006 | 0.4173 |
| 1997.00 | 1.0121 | 0.9503 | 0.3201 |
| 2169.00 | 3.3103 | 0.0503 | 0.1531 |
| 2169.00 | 3.3103 | 0.1006 | 0.2246 |
| 2169.00 | 3.3103 | 0.1509 | 0.2545 |
| 2169.00 | 3.3103 | 0.2011 | 0.2849 |
| 2169.00 | 3.3103 | 0.2513 | 0.3150 |
| 2169.00 | 3.3103 | 0.3015 | 0.3420 |
| 2169.00 | 3.3103 | 0.4017 | 0.3874 |
| 2169.00 | 3.3103 | 0.5018 | 0.4191 |
| 2169.00 | 3.3103 | 0.6017 | 0.4434 |
| 2169.00 | 3.3103 | 0.6516 | 0.4420 |
| 2169.00 | 3.3103 | 0.7015 | 0.4387 |
| 2169.00 | 3.3103 | 0.8011 | 0.4100 |
| 2169.00 | 3.3103 | 0.9006 | 0.3315 |
| 2169.00 | 3.3103 | 0.9503 | 0.2225 |
| 3897.00 | 1.0121 | 0.0509 | 0.1297 |
| 3897.00 | 1.0121 | 0.1008 | 0.2323 |
| 3897.00 | 1.0121 | 0.1511 | 0.3103 |
| 3897.00 | 1.0121 | 0.2014 | 0.3692 |
| 3897.00 | 1.0121 | 0.2517 | 0.4114 |
| 3897.00 | 1.0121 | 0.3019 | 0.4432 |
| 3897.00 | 1.0121 | 0.4021 | 0.4803 |
| 3897.00 | 1.0121 | 0.5022 | 0.5130 |
| 3897.00 | 1.0121 | 0.6021 | 0.5466 |
| 3897.00 | 1.0121 | 0.6520 | 0.5506 |
| 3897.00 | 1.0121 | 0.7019 | 0.5483 |
| 3897.00 | 1.0121 | 0.8014 | 0.5124 |
| 3897.00 | 1.0121 | 0.9008 | 0.4103 |
| 3897.00 | 1.0121 | 0.9504 | 0.3044 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Pressure, kPa = 3980 (Liquid)
- Solvent: Amount ratio of component to other component of binary solvent = 1.004 (Liquid)
- Temperature, K = 323.15 (Liquid)
| Mole fraction of Propene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0509 | 0.1469 |
| 0.1016 | 0.2607 |
| 0.1523 | 0.3465 |
| 0.2029 | 0.4092 |
| 0.2534 | 0.4615 |
| 0.3038 | 0.4960 |
| 0.4044 | 0.5411 |
| 0.5065 | 0.5769 |
| 0.6044 | 0.6016 |
| 0.6541 | 0.6092 |
| 0.7038 | 0.6046 |
| 0.8029 | 0.5719 |
| 0.9016 | 0.4483 |
| 0.9509 | 0.3150 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Temperature, K = 333.15 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Pressure, kPa - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Water (3) - Liquid | Mole fraction of Propene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 3975.00 | 1.004 | 0.0507 | 0.1577 |
| 3975.00 | 1.004 | 0.1013 | 0.2879 |
| 3975.00 | 1.004 | 0.1519 | 0.3840 |
| 3975.00 | 1.004 | 0.2023 | 0.4548 |
| 3975.00 | 1.004 | 0.2527 | 0.5108 |
| 3975.00 | 1.004 | 0.3031 | 0.5472 |
| 3975.00 | 1.004 | 0.3533 | 0.5766 |
| 3975.00 | 1.004 | 0.4035 | 0.6036 |
| 3975.00 | 1.004 | 0.5036 | 0.6514 |
| 3975.00 | 1.004 | 0.6035 | 0.6842 |
| 3975.00 | 1.004 | 0.7030 | 0.6982 |
| 3975.00 | 1.004 | 0.7527 | 0.6937 |
| 3975.00 | 1.004 | 0.8023 | 0.6713 |
| 3975.00 | 1.004 | 0.9013 | 0.5366 |
| 3975.00 | 1.004 | 0.9507 | 0.3874 |
| 3980.00 | 3.298 | 0.0506 | 0.1269 |
| 3980.00 | 3.298 | 0.1011 | 0.2514 |
| 3980.00 | 3.298 | 0.1516 | 0.3583 |
| 3980.00 | 3.298 | 0.2020 | 0.4571 |
| 3980.00 | 3.298 | 0.2523 | 0.5423 |
| 3980.00 | 3.298 | 0.3026 | 0.6200 |
| 3980.00 | 3.298 | 0.3528 | 0.6877 |
| 3980.00 | 3.298 | 0.4030 | 0.7430 |
| 3980.00 | 3.298 | 0.4531 | 0.7915 |
| 3980.00 | 3.298 | 0.5031 | 0.8289 |
| 3980.00 | 3.298 | 0.5531 | 0.8551 |
| 3980.00 | 3.298 | 0.6030 | 0.8741 |
| 3980.00 | 3.298 | 0.7026 | 0.8827 |
| 3980.00 | 3.298 | 0.8020 | 0.8384 |
| 3980.00 | 3.298 | 0.9011 | 0.6495 |
| 3980.00 | 3.329 | 0.1010 | 0.2259 |
| 3980.00 | 3.329 | 0.2018 | 0.3164 |
| 3980.00 | 3.329 | 0.3024 | 0.3922 |
| 3980.00 | 3.329 | 0.3526 | 0.4262 |
| 3980.00 | 3.329 | 0.4027 | 0.4545 |
| 3980.00 | 3.329 | 0.4528 | 0.4833 |
| 3980.00 | 3.329 | 0.5029 | 0.5073 |
| 3980.00 | 3.329 | 0.5528 | 0.5269 |
| 3980.00 | 3.329 | 0.6027 | 0.5412 |
| 3980.00 | 3.329 | 0.6526 | 0.5490 |
| 3980.00 | 3.329 | 0.7024 | 0.5501 |
| 3980.00 | 3.329 | 0.8018 | 0.5133 |
| 3980.00 | 3.329 | 0.9010 | 0.3790 |
| 3980.00 | 3.329 | 0.3526 | 0.4243 |
| 5890.00 | 3.329 | 0.0406 | 0.1607 |
| 5890.00 | 3.329 | 0.0711 | 0.2079 |
| 5890.00 | 3.329 | 0.1015 | 0.2457 |
| 5890.00 | 3.329 | 0.1521 | 0.2947 |
| 5890.00 | 3.329 | 0.2026 | 0.3484 |
| 5890.00 | 3.329 | 0.3537 | 0.4675 |
| 5890.00 | 3.329 | 0.4540 | 0.5258 |
| 5890.00 | 3.329 | 0.5540 | 0.5659 |
| 5890.00 | 3.329 | 0.6039 | 0.5798 |
| 5890.00 | 3.329 | 0.6537 | 0.5854 |
| 5890.00 | 3.329 | 0.7034 | 0.5816 |
| 5890.00 | 3.329 | 0.8026 | 0.5351 |
| 5890.00 | 3.329 | 0.8521 | 0.4643 |
| 5890.00 | 3.329 | 0.9014 | 0.3872 |
| 5890.00 | 3.329 | 0.9409 | 0.2836 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Temperature, K = 313.15 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Pressure, kPa - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Water (3) - Liquid | Mole fraction of Propene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 1997.00 | 1.0121 | 0.0503 | 0.1317 |
| 1997.00 | 1.0121 | 0.1006 | 0.2347 |
| 1997.00 | 1.0121 | 0.1508 | 0.3104 |
| 1997.00 | 1.0121 | 0.2010 | 0.3651 |
| 1997.00 | 1.0121 | 0.2512 | 0.4043 |
| 1997.00 | 1.0121 | 0.3013 | 0.4298 |
| 1997.00 | 1.0121 | 0.4015 | 0.4707 |
| 1997.00 | 1.0121 | 0.5016 | 0.5018 |
| 1997.00 | 1.0121 | 0.6015 | 0.5248 |
| 1997.00 | 1.0121 | 0.6514 | 0.5298 |
| 1997.00 | 1.0121 | 0.7013 | 0.5316 |
| 1997.00 | 1.0121 | 0.8010 | 0.5147 |
| 1997.00 | 1.0121 | 0.9006 | 0.4173 |
| 1997.00 | 1.0121 | 0.9503 | 0.3201 |
| 2169.00 | 3.3103 | 0.0503 | 0.1531 |
| 2169.00 | 3.3103 | 0.1006 | 0.2246 |
| 2169.00 | 3.3103 | 0.1509 | 0.2545 |
| 2169.00 | 3.3103 | 0.2011 | 0.2849 |
| 2169.00 | 3.3103 | 0.2513 | 0.3150 |
| 2169.00 | 3.3103 | 0.3015 | 0.3420 |
| 2169.00 | 3.3103 | 0.4017 | 0.3874 |
| 2169.00 | 3.3103 | 0.5018 | 0.4191 |
| 2169.00 | 3.3103 | 0.6017 | 0.4434 |
| 2169.00 | 3.3103 | 0.6516 | 0.4420 |
| 2169.00 | 3.3103 | 0.7015 | 0.4387 |
| 2169.00 | 3.3103 | 0.8011 | 0.4100 |
| 2169.00 | 3.3103 | 0.9006 | 0.3315 |
| 2169.00 | 3.3103 | 0.9503 | 0.2225 |
| 3897.00 | 1.0121 | 0.0509 | 0.1297 |
| 3897.00 | 1.0121 | 0.1008 | 0.2323 |
| 3897.00 | 1.0121 | 0.1511 | 0.3103 |
| 3897.00 | 1.0121 | 0.2014 | 0.3692 |
| 3897.00 | 1.0121 | 0.2517 | 0.4114 |
| 3897.00 | 1.0121 | 0.3019 | 0.4432 |
| 3897.00 | 1.0121 | 0.4021 | 0.4803 |
| 3897.00 | 1.0121 | 0.5022 | 0.5130 |
| 3897.00 | 1.0121 | 0.6021 | 0.5466 |
| 3897.00 | 1.0121 | 0.6520 | 0.5506 |
| 3897.00 | 1.0121 | 0.7019 | 0.5483 |
| 3897.00 | 1.0121 | 0.8014 | 0.5124 |
| 3897.00 | 1.0121 | 0.9008 | 0.4103 |
| 3897.00 | 1.0121 | 0.9504 | 0.3044 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Pressure, kPa = 3980 (Liquid)
- Solvent: Amount ratio of component to other component of binary solvent = 1.004 (Liquid)
- Temperature, K = 323.15 (Liquid)
| Mole fraction of Propene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0509 | 0.1469 |
| 0.1016 | 0.2607 |
| 0.1523 | 0.3465 |
| 0.2029 | 0.4092 |
| 0.2534 | 0.4615 |
| 0.3038 | 0.4960 |
| 0.4044 | 0.5411 |
| 0.5065 | 0.5769 |
| 0.6044 | 0.6016 |
| 0.6541 | 0.6092 |
| 0.7038 | 0.6046 |
| 0.8029 | 0.5719 |
| 0.9016 | 0.4483 |
| 0.9509 | 0.3150 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Temperature, K = 333.15 (Liquid)
| Fixed | Measured | ||
|---|---|---|---|
| Pressure, kPa - Liquid | Solvent: Amount ratio of component to other component of binary solvent of Water (3) - Liquid | Mole fraction of Propene (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 3975.00 | 1.004 | 0.0507 | 0.1577 |
| 3975.00 | 1.004 | 0.1013 | 0.2879 |
| 3975.00 | 1.004 | 0.1519 | 0.3840 |
| 3975.00 | 1.004 | 0.2023 | 0.4548 |
| 3975.00 | 1.004 | 0.2527 | 0.5108 |
| 3975.00 | 1.004 | 0.3031 | 0.5472 |
| 3975.00 | 1.004 | 0.3533 | 0.5766 |
| 3975.00 | 1.004 | 0.4035 | 0.6036 |
| 3975.00 | 1.004 | 0.5036 | 0.6514 |
| 3975.00 | 1.004 | 0.6035 | 0.6842 |
| 3975.00 | 1.004 | 0.7030 | 0.6982 |
| 3975.00 | 1.004 | 0.7527 | 0.6937 |
| 3975.00 | 1.004 | 0.8023 | 0.6713 |
| 3975.00 | 1.004 | 0.9013 | 0.5366 |
| 3975.00 | 1.004 | 0.9507 | 0.3874 |
| 3980.00 | 3.298 | 0.0506 | 0.1269 |
| 3980.00 | 3.298 | 0.1011 | 0.2514 |
| 3980.00 | 3.298 | 0.1516 | 0.3583 |
| 3980.00 | 3.298 | 0.2020 | 0.4571 |
| 3980.00 | 3.298 | 0.2523 | 0.5423 |
| 3980.00 | 3.298 | 0.3026 | 0.6200 |
| 3980.00 | 3.298 | 0.3528 | 0.6877 |
| 3980.00 | 3.298 | 0.4030 | 0.7430 |
| 3980.00 | 3.298 | 0.4531 | 0.7915 |
| 3980.00 | 3.298 | 0.5031 | 0.8289 |
| 3980.00 | 3.298 | 0.5531 | 0.8551 |
| 3980.00 | 3.298 | 0.6030 | 0.8741 |
| 3980.00 | 3.298 | 0.7026 | 0.8827 |
| 3980.00 | 3.298 | 0.8020 | 0.8384 |
| 3980.00 | 3.298 | 0.9011 | 0.6495 |
| 3980.00 | 3.329 | 0.1010 | 0.2259 |
| 3980.00 | 3.329 | 0.2018 | 0.3164 |
| 3980.00 | 3.329 | 0.3024 | 0.3922 |
| 3980.00 | 3.329 | 0.3526 | 0.4262 |
| 3980.00 | 3.329 | 0.4027 | 0.4545 |
| 3980.00 | 3.329 | 0.4528 | 0.4833 |
| 3980.00 | 3.329 | 0.5029 | 0.5073 |
| 3980.00 | 3.329 | 0.5528 | 0.5269 |
| 3980.00 | 3.329 | 0.6027 | 0.5412 |
| 3980.00 | 3.329 | 0.6526 | 0.5490 |
| 3980.00 | 3.329 | 0.7024 | 0.5501 |
| 3980.00 | 3.329 | 0.8018 | 0.5133 |
| 3980.00 | 3.329 | 0.9010 | 0.3790 |
| 3980.00 | 3.329 | 0.3526 | 0.4243 |
| 5890.00 | 3.329 | 0.0406 | 0.1607 |
| 5890.00 | 3.329 | 0.0711 | 0.2079 |
| 5890.00 | 3.329 | 0.1015 | 0.2457 |
| 5890.00 | 3.329 | 0.1521 | 0.2947 |
| 5890.00 | 3.329 | 0.2026 | 0.3484 |
| 5890.00 | 3.329 | 0.3537 | 0.4675 |
| 5890.00 | 3.329 | 0.4540 | 0.5258 |
| 5890.00 | 3.329 | 0.5540 | 0.5659 |
| 5890.00 | 3.329 | 0.6039 | 0.5798 |
| 5890.00 | 3.329 | 0.6537 | 0.5854 |
| 5890.00 | 3.329 | 0.7034 | 0.5816 |
| 5890.00 | 3.329 | 0.8026 | 0.5351 |
| 5890.00 | 3.329 | 0.8521 | 0.4643 |
| 5890.00 | 3.329 | 0.9014 | 0.3872 |
| 5890.00 | 3.329 | 0.9409 | 0.2836 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.0904 (Liquid)
- Mole fraction = 0.3697 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 305.05 | 481.00 | 805.22 |
| 305.05 | 799.90 | 805.53 |
| 305.05 | 1118.90 | 805.81 |
| 305.05 | 1587.30 | 806.21 |
| 305.05 | 1973.80 | 806.57 |
| 305.05 | 2343.70 | 806.88 |
| 305.05 | 2861.60 | 807.33 |
| 305.05 | 3088.90 | 807.54 |
| 305.05 | 3620.10 | 807.99 |
| 305.05 | 3948.40 | 808.27 |
| 305.05 | 4345.40 | 808.61 |
| 305.05 | 4751.00 | 808.95 |
| 305.05 | 5150.70 | 809.29 |
| 305.05 | 5557.60 | 809.63 |
| 305.05 | 5964.40 | 809.96 |
| 305.05 | 6366.60 | 810.3 |
| 305.05 | 6786.60 | 810.64 |
| 305.05 | 7207.10 | 810.99 |
| 305.05 | 7609.10 | 811.32 |
| 305.05 | 8028.60 | 811.65 |
| 305.05 | 8459.00 | 812.01 |
| 305.05 | 8872.40 | 812.34 |
| 305.05 | 9272.30 | 812.66 |
| 305.05 | 9679.10 | 812.99 |
| 305.05 | 10068.40 | 813.35 |
| 325.13 | 1096.50 | 787.78 |
| 325.13 | 1376.50 | 788.08 |
| 325.13 | 1788.40 | 788.5 |
| 325.13 | 2205.50 | 788.92 |
| 325.13 | 2525.60 | 789.26 |
| 325.13 | 2916.90 | 789.68 |
| 325.13 | 3385.30 | 790.18 |
| 325.13 | 3725.20 | 790.51 |
| 325.13 | 4135.30 | 790.9 |
| 325.13 | 4548.30 | 791.31 |
| 325.13 | 4942.80 | 791.7 |
| 325.13 | 5352.40 | 792.1 |
| 325.13 | 5817.10 | 792.53 |
| 325.13 | 6158.80 | 792.87 |
| 325.13 | 6571.30 | 793.27 |
| 325.13 | 6970.60 | 793.68 |
| 325.13 | 7361.10 | 794.07 |
| 325.13 | 7752.50 | 794.47 |
| 325.13 | 8126.30 | 794.84 |
| 325.13 | 8556.30 | 795.24 |
| 325.13 | 8951.40 | 795.67 |
| 325.13 | 9359.70 | 796.03 |
| 325.13 | 9783.20 | 796.45 |
| 325.13 | 10193.30 | 796.86 |
| 350.16 | 1979.40 | 760.95 |
| 350.16 | 2250.60 | 761.47 |
| 350.16 | 2653.20 | 762.19 |
| 350.16 | 2789.40 | 762.47 |
| 350.16 | 3172.50 | 763.0 |
| 350.16 | 3487.70 | 763.47 |
| 350.16 | 3819.20 | 763.99 |
| 350.16 | 4171.50 | 764.47 |
| 350.16 | 4558.70 | 764.96 |
| 350.16 | 4903.60 | 765.44 |
| 350.16 | 5272.70 | 765.96 |
| 350.16 | 5605.20 | 766.43 |
| 350.16 | 5992.70 | 766.93 |
| 350.16 | 6388.60 | 767.42 |
| 350.16 | 6753.50 | 767.93 |
| 350.16 | 7175.10 | 768.45 |
| 350.16 | 7534.00 | 768.95 |
| 350.16 | 7886.20 | 769.36 |
| 350.16 | 8290.30 | 769.86 |
| 350.16 | 8702.30 | 770.37 |
| 350.16 | 8988.40 | 770.84 |
| 350.16 | 9371.90 | 771.35 |
| 350.16 | 9692.90 | 771.8 |
| 350.16 | 10018.70 | 772.34 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.1828 (Liquid)
- Mole fraction = 0.3828 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 300.10 | 1019.90 | 758.54 |
| 300.10 | 1335.50 | 758.91 |
| 300.10 | 1692.50 | 759.33 |
| 300.10 | 2068.40 | 759.75 |
| 300.10 | 2506.80 | 760.25 |
| 300.10 | 2823.30 | 760.61 |
| 300.10 | 3266.50 | 761.1 |
| 300.10 | 3565.00 | 761.44 |
| 300.10 | 3910.00 | 761.82 |
| 300.10 | 4361.30 | 762.31 |
| 300.10 | 4679.80 | 762.67 |
| 300.10 | 5064.10 | 763.09 |
| 300.10 | 5454.10 | 763.51 |
| 300.10 | 5850.30 | 763.93 |
| 300.10 | 6327.20 | 764.42 |
| 300.10 | 6622.80 | 764.75 |
| 300.10 | 6954.30 | 765.1 |
| 300.10 | 7456.60 | 765.62 |
| 300.10 | 7843.90 | 766.01 |
| 300.10 | 8237.90 | 766.41 |
| 300.10 | 8640.80 | 766.82 |
| 300.10 | 9064.10 | 767.26 |
| 300.10 | 9470.50 | 767.67 |
| 300.10 | 9858.30 | 768.09 |
| 325.11 | 1872.80 | 738.13 |
| 325.11 | 2272.30 | 738.62 |
| 325.11 | 2564.80 | 739.03 |
| 325.11 | 2842.50 | 739.43 |
| 325.11 | 3163.60 | 740.0 |
| 325.11 | 3460.30 | 740.41 |
| 325.11 | 3802.10 | 740.8 |
| 325.11 | 4205.50 | 741.3 |
| 325.11 | 4570.50 | 741.79 |
| 325.11 | 4912.10 | 742.16 |
| 325.11 | 5330.40 | 742.65 |
| 325.11 | 5702.30 | 743.08 |
| 325.11 | 6069.10 | 743.56 |
| 325.11 | 6403.00 | 743.98 |
| 325.11 | 6776.10 | 744.45 |
| 325.11 | 7099.20 | 744.86 |
| 325.11 | 7495.70 | 745.33 |
| 325.11 | 7840.20 | 745.77 |
| 325.11 | 8217.30 | 746.22 |
| 325.11 | 8572.10 | 746.68 |
| 325.11 | 8934.60 | 747.14 |
| 325.11 | 9271.10 | 747.56 |
| 325.11 | 9620.80 | 747.98 |
| 325.11 | 10045.40 | 748.47 |
| 345.10 | 2298.40 | 718.81 |
| 345.10 | 2347.50 | 718.97 |
| 345.10 | 2730.70 | 719.58 |
| 345.10 | 2993.90 | 720.06 |
| 345.10 | 3284.20 | 720.53 |
| 345.10 | 3545.40 | 720.93 |
| 345.10 | 3953.70 | 721.63 |
| 345.10 | 4112.50 | 721.93 |
| 345.10 | 4426.00 | 722.46 |
| 345.10 | 4706.40 | 722.89 |
| 345.10 | 5000.90 | 723.31 |
| 345.10 | 5282.10 | 723.84 |
| 345.10 | 5590.20 | 724.3 |
| 345.10 | 5944.60 | 724.83 |
| 345.10 | 6183.30 | 725.19 |
| 345.10 | 6485.90 | 725.68 |
| 345.10 | 6790.40 | 726.18 |
| 345.10 | 7088.30 | 726.63 |
| 345.10 | 7396.10 | 727.11 |
| 345.10 | 7697.50 | 727.55 |
| 345.10 | 8010.40 | 728.03 |
| 345.10 | 8324.50 | 728.51 |
| 345.10 | 8635.00 | 728.98 |
| 345.10 | 8947.20 | 729.42 |
| 345.10 | 9276.00 | 729.9 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.3031 (Liquid)
- Mole fraction = 0.5024 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 300.10 | 930.90 | 707.92 |
| 300.10 | 1197.00 | 708.29 |
| 300.10 | 1556.10 | 708.78 |
| 300.10 | 1948.10 | 709.29 |
| 300.10 | 2458.80 | 709.93 |
| 300.10 | 2780.10 | 710.37 |
| 300.10 | 3164.50 | 710.88 |
| 300.10 | 3512.80 | 711.35 |
| 300.10 | 4009.00 | 711.99 |
| 300.10 | 4360.40 | 712.44 |
| 300.10 | 4766.30 | 712.95 |
| 300.10 | 5154.60 | 713.45 |
| 300.10 | 5580.50 | 713.98 |
| 300.10 | 5973.40 | 714.47 |
| 300.10 | 6437.40 | 715.04 |
| 300.10 | 6813.90 | 715.51 |
| 300.10 | 7245.70 | 716.02 |
| 300.10 | 7676.20 | 716.54 |
| 300.10 | 8095.30 | 717.04 |
| 300.10 | 8527.10 | 717.54 |
| 300.10 | 9025.90 | 718.13 |
| 300.10 | 9429.00 | 718.61 |
| 300.10 | 9785.50 | 719.09 |
| 300.10 | 10213.80 | 719.6 |
| 325.13 | 1187.00 | 678.16 |
| 325.13 | 1443.20 | 678.62 |
| 325.13 | 1727.80 | 679.11 |
| 325.13 | 2143.60 | 679.8 |
| 325.13 | 2479.70 | 680.35 |
| 325.13 | 2891.40 | 681.1 |
| 325.13 | 3154.40 | 681.59 |
| 325.13 | 3531.80 | 682.22 |
| 325.13 | 3834.40 | 682.74 |
| 325.13 | 4104.10 | 683.18 |
| 325.13 | 4552.90 | 683.87 |
| 325.13 | 4913.70 | 684.44 |
| 325.13 | 5291.60 | 685.03 |
| 325.13 | 5673.00 | 685.61 |
| 325.13 | 6031.10 | 686.15 |
| 325.13 | 6401.70 | 686.72 |
| 325.13 | 6789.20 | 687.28 |
| 325.13 | 7173.60 | 687.86 |
| 325.13 | 7569.00 | 688.43 |
| 325.13 | 7965.20 | 689.02 |
| 325.13 | 8355.00 | 689.57 |
| 325.13 | 8763.70 | 690.16 |
| 325.13 | 9170.70 | 690.73 |
| 325.13 | 9574.80 | 691.28 |
| 325.13 | 9969.40 | 691.84 |
| 350.13 | 2436.80 | 653.52 |
| 350.13 | 2604.80 | 653.96 |
| 350.13 | 2930.10 | 654.68 |
| 350.13 | 3202.50 | 655.27 |
| 350.13 | 3734.40 | 656.44 |
| 350.13 | 3872.40 | 656.79 |
| 350.13 | 4136.90 | 657.4 |
| 350.13 | 4488.90 | 658.17 |
| 350.13 | 4810.50 | 658.86 |
| 350.13 | 5126.00 | 659.5 |
| 350.13 | 5445.20 | 660.17 |
| 350.13 | 5766.20 | 660.85 |
| 350.13 | 6092.80 | 661.51 |
| 350.13 | 6419.00 | 662.19 |
| 350.13 | 6762.00 | 662.87 |
| 350.13 | 7090.70 | 663.5 |
| 350.13 | 7423.40 | 664.19 |
| 350.13 | 7773.10 | 664.87 |
| 350.13 | 8125.80 | 665.54 |
| 350.13 | 8476.00 | 666.19 |
| 350.13 | 8829.50 | 666.84 |
| 350.13 | 9190.50 | 667.56 |
| 350.13 | 9544.70 | 668.2 |
| 350.13 | 9902.40 | 668.83 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.3906 (Liquid)
- Mole fraction = 0.4236 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 300.10 | 1018.70 | 680.98 |
| 300.10 | 1199.80 | 681.27 |
| 300.10 | 1620.90 | 681.88 |
| 300.10 | 1977.30 | 682.39 |
| 300.10 | 2327.90 | 682.91 |
| 300.10 | 2703.90 | 683.48 |
| 300.10 | 3029.60 | 683.95 |
| 300.10 | 3363.30 | 684.43 |
| 300.10 | 3758.10 | 685.0 |
| 300.10 | 4032.30 | 685.37 |
| 300.10 | 4487.20 | 686.01 |
| 300.10 | 4841.40 | 686.51 |
| 300.10 | 5211.20 | 687.02 |
| 300.10 | 5591.90 | 687.54 |
| 300.10 | 5957.50 | 688.05 |
| 300.10 | 6330.70 | 688.56 |
| 300.10 | 6708.40 | 689.06 |
| 300.10 | 7081.10 | 689.56 |
| 300.10 | 7464.90 | 690.07 |
| 300.10 | 7865.50 | 690.59 |
| 300.10 | 8251.90 | 691.1 |
| 300.10 | 8631.30 | 691.6 |
| 300.10 | 9014.00 | 692.09 |
| 300.10 | 9422.90 | 692.6 |
| 300.10 | 9832.40 | 693.12 |
| 325.11 | 1951.80 | 650.66 |
| 325.11 | 2356.10 | 651.45 |
| 325.11 | 2596.00 | 651.95 |
| 325.11 | 2934.10 | 652.61 |
| 325.11 | 3207.70 | 653.19 |
| 325.11 | 3493.80 | 653.75 |
| 325.11 | 3878.70 | 654.46 |
| 325.11 | 4223.40 | 655.08 |
| 325.11 | 4567.90 | 655.73 |
| 325.11 | 4892.60 | 656.32 |
| 325.11 | 5223.50 | 656.91 |
| 325.11 | 5558.60 | 657.52 |
| 325.11 | 5927.30 | 658.17 |
| 325.11 | 6278.00 | 658.79 |
| 325.11 | 6659.60 | 659.45 |
| 325.11 | 7005.10 | 660.05 |
| 325.11 | 7364.50 | 660.65 |
| 325.11 | 7730.70 | 661.26 |
| 325.11 | 8119.20 | 661.9 |
| 325.11 | 8474.30 | 662.48 |
| 325.11 | 8857.20 | 663.1 |
| 325.11 | 9233.60 | 663.72 |
| 325.11 | 9619.20 | 664.33 |
| 325.11 | 9971.40 | 664.93 |
| 350.11 | 2620.50 | 618.74 |
| 350.11 | 3007.20 | 619.87 |
| 350.11 | 3183.00 | 620.39 |
| 350.11 | 3528.10 | 621.38 |
| 350.11 | 3731.20 | 621.97 |
| 350.11 | 4088.40 | 622.82 |
| 350.11 | 4364.50 | 623.63 |
| 350.11 | 4653.60 | 624.39 |
| 350.11 | 4951.20 | 625.19 |
| 350.11 | 5258.20 | 625.98 |
| 350.11 | 5596.80 | 626.78 |
| 350.11 | 5945.80 | 627.64 |
| 350.11 | 6238.20 | 628.34 |
| 350.11 | 6568.00 | 629.17 |
| 350.11 | 6882.80 | 629.92 |
| 350.11 | 7201.80 | 630.66 |
| 350.11 | 7561.10 | 631.49 |
| 350.11 | 7908.70 | 632.29 |
| 350.11 | 8235.70 | 633.07 |
| 350.11 | 8584.70 | 633.86 |
| 350.11 | 8912.60 | 634.62 |
| 350.11 | 9291.10 | 635.35 |
| 350.11 | 9665.90 | 636.22 |
| 350.11 | 9987.40 | 636.95 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.6123 (Liquid)
- Mole fraction = 0.3039 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 300.10 | 1085.40 | 614.94 |
| 300.10 | 1531.40 | 615.81 |
| 300.10 | 1870.70 | 616.53 |
| 300.10 | 2372.60 | 617.48 |
| 300.10 | 2527.20 | 617.84 |
| 300.10 | 2922.10 | 618.61 |
| 300.10 | 3226.20 | 619.19 |
| 300.10 | 3579.40 | 619.86 |
| 300.10 | 4068.20 | 620.74 |
| 300.10 | 4281.70 | 621.17 |
| 300.10 | 4729.00 | 622.0 |
| 300.10 | 5109.50 | 622.68 |
| 300.10 | 5494.50 | 623.39 |
| 300.10 | 5875.10 | 624.07 |
| 300.10 | 6252.10 | 624.73 |
| 300.10 | 6636.50 | 625.4 |
| 300.10 | 7032.90 | 626.07 |
| 300.10 | 7453.40 | 626.76 |
| 300.10 | 7866.20 | 627.47 |
| 300.10 | 8255.70 | 628.11 |
| 300.10 | 8661.90 | 628.75 |
| 300.10 | 9079.60 | 629.46 |
| 300.10 | 9474.20 | 630.08 |
| 300.10 | 9896.70 | 630.79 |
| 325.12 | 1894.10 | 580.11 |
| 325.12 | 2207.30 | 580.96 |
| 325.12 | 2528.10 | 581.84 |
| 325.12 | 2847.40 | 582.67 |
| 325.12 | 3200.80 | 583.61 |
| 325.12 | 3499.10 | 584.39 |
| 325.12 | 3778.00 | 585.12 |
| 325.12 | 3817.50 | 586.14 |
| 325.12 | 4214.20 | 587.19 |
| 325.12 | 4522.10 | 587.93 |
| 325.12 | 4866.30 | 588.81 |
| 325.12 | 5210.20 | 589.63 |
| 325.12 | 5562.90 | 590.47 |
| 325.12 | 5930.30 | 591.32 |
| 325.12 | 6321.20 | 592.2 |
| 325.12 | 6686.30 | 593.02 |
| 325.12 | 7057.50 | 593.82 |
| 325.12 | 7468.80 | 594.69 |
| 325.12 | 7876.20 | 595.54 |
| 325.12 | 8253.60 | 596.34 |
| 325.12 | 8653.20 | 597.15 |
| 325.12 | 9078.40 | 597.99 |
| 325.12 | 9500.10 | 598.83 |
| 325.12 | 9915.50 | 599.65 |
| 350.10 | 2850.10 | 540.02 |
| 350.10 | 3016.80 | 540.87 |
| 350.10 | 3231.50 | 541.94 |
| 350.10 | 3505.70 | 543.11 |
| 350.10 | 3782.70 | 544.27 |
| 350.10 | 3996.50 | 545.27 |
| 350.10 | 4328.10 | 546.57 |
| 350.10 | 4621.10 | 547.8 |
| 350.10 | 4866.70 | 548.79 |
| 350.10 | 5169.30 | 550.07 |
| 350.10 | 5457.30 | 551.09 |
| 350.10 | 5759.20 | 552.24 |
| 350.10 | 6094.30 | 553.32 |
| 350.10 | 6419.10 | 554.43 |
| 350.10 | 6732.10 | 555.54 |
| 350.10 | 7048.00 | 556.69 |
| 350.10 | 7372.90 | 557.82 |
| 350.10 | 7703.00 | 558.93 |
| 350.10 | 8059.80 | 559.96 |
| 350.10 | 8438.50 | 561.12 |
| 350.10 | 8820.80 | 562.37 |
| 350.10 | 9187.70 | 563.44 |
| 350.10 | 9575.50 | 564.54 |
| 350.10 | 9939.10 | 565.57 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.0904 (Liquid)
- Mole fraction = 0.3697 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 305.05 | 481.00 | 805.22 |
| 305.05 | 799.90 | 805.53 |
| 305.05 | 1118.90 | 805.81 |
| 305.05 | 1587.30 | 806.21 |
| 305.05 | 1973.80 | 806.57 |
| 305.05 | 2343.70 | 806.88 |
| 305.05 | 2861.60 | 807.33 |
| 305.05 | 3088.90 | 807.54 |
| 305.05 | 3620.10 | 807.99 |
| 305.05 | 3948.40 | 808.27 |
| 305.05 | 4345.40 | 808.61 |
| 305.05 | 4751.00 | 808.95 |
| 305.05 | 5150.70 | 809.29 |
| 305.05 | 5557.60 | 809.63 |
| 305.05 | 5964.40 | 809.96 |
| 305.05 | 6366.60 | 810.3 |
| 305.05 | 6786.60 | 810.64 |
| 305.05 | 7207.10 | 810.99 |
| 305.05 | 7609.10 | 811.32 |
| 305.05 | 8028.60 | 811.65 |
| 305.05 | 8459.00 | 812.01 |
| 305.05 | 8872.40 | 812.34 |
| 305.05 | 9272.30 | 812.66 |
| 305.05 | 9679.10 | 812.99 |
| 305.05 | 10068.40 | 813.35 |
| 325.13 | 1096.50 | 787.78 |
| 325.13 | 1376.50 | 788.08 |
| 325.13 | 1788.40 | 788.5 |
| 325.13 | 2205.50 | 788.92 |
| 325.13 | 2525.60 | 789.26 |
| 325.13 | 2916.90 | 789.68 |
| 325.13 | 3385.30 | 790.18 |
| 325.13 | 3725.20 | 790.51 |
| 325.13 | 4135.30 | 790.9 |
| 325.13 | 4548.30 | 791.31 |
| 325.13 | 4942.80 | 791.7 |
| 325.13 | 5352.40 | 792.1 |
| 325.13 | 5817.10 | 792.53 |
| 325.13 | 6158.80 | 792.87 |
| 325.13 | 6571.30 | 793.27 |
| 325.13 | 6970.60 | 793.68 |
| 325.13 | 7361.10 | 794.07 |
| 325.13 | 7752.50 | 794.47 |
| 325.13 | 8126.30 | 794.84 |
| 325.13 | 8556.30 | 795.24 |
| 325.13 | 8951.40 | 795.67 |
| 325.13 | 9359.70 | 796.03 |
| 325.13 | 9783.20 | 796.45 |
| 325.13 | 10193.30 | 796.86 |
| 350.16 | 1979.40 | 760.95 |
| 350.16 | 2250.60 | 761.47 |
| 350.16 | 2653.20 | 762.19 |
| 350.16 | 2789.40 | 762.47 |
| 350.16 | 3172.50 | 763.0 |
| 350.16 | 3487.70 | 763.47 |
| 350.16 | 3819.20 | 763.99 |
| 350.16 | 4171.50 | 764.47 |
| 350.16 | 4558.70 | 764.96 |
| 350.16 | 4903.60 | 765.44 |
| 350.16 | 5272.70 | 765.96 |
| 350.16 | 5605.20 | 766.43 |
| 350.16 | 5992.70 | 766.93 |
| 350.16 | 6388.60 | 767.42 |
| 350.16 | 6753.50 | 767.93 |
| 350.16 | 7175.10 | 768.45 |
| 350.16 | 7534.00 | 768.95 |
| 350.16 | 7886.20 | 769.36 |
| 350.16 | 8290.30 | 769.86 |
| 350.16 | 8702.30 | 770.37 |
| 350.16 | 8988.40 | 770.84 |
| 350.16 | 9371.90 | 771.35 |
| 350.16 | 9692.90 | 771.8 |
| 350.16 | 10018.70 | 772.34 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.1828 (Liquid)
- Mole fraction = 0.3828 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 300.10 | 1019.90 | 758.54 |
| 300.10 | 1335.50 | 758.91 |
| 300.10 | 1692.50 | 759.33 |
| 300.10 | 2068.40 | 759.75 |
| 300.10 | 2506.80 | 760.25 |
| 300.10 | 2823.30 | 760.61 |
| 300.10 | 3266.50 | 761.1 |
| 300.10 | 3565.00 | 761.44 |
| 300.10 | 3910.00 | 761.82 |
| 300.10 | 4361.30 | 762.31 |
| 300.10 | 4679.80 | 762.67 |
| 300.10 | 5064.10 | 763.09 |
| 300.10 | 5454.10 | 763.51 |
| 300.10 | 5850.30 | 763.93 |
| 300.10 | 6327.20 | 764.42 |
| 300.10 | 6622.80 | 764.75 |
| 300.10 | 6954.30 | 765.1 |
| 300.10 | 7456.60 | 765.62 |
| 300.10 | 7843.90 | 766.01 |
| 300.10 | 8237.90 | 766.41 |
| 300.10 | 8640.80 | 766.82 |
| 300.10 | 9064.10 | 767.26 |
| 300.10 | 9470.50 | 767.67 |
| 300.10 | 9858.30 | 768.09 |
| 325.11 | 1872.80 | 738.13 |
| 325.11 | 2272.30 | 738.62 |
| 325.11 | 2564.80 | 739.03 |
| 325.11 | 2842.50 | 739.43 |
| 325.11 | 3163.60 | 740.0 |
| 325.11 | 3460.30 | 740.41 |
| 325.11 | 3802.10 | 740.8 |
| 325.11 | 4205.50 | 741.3 |
| 325.11 | 4570.50 | 741.79 |
| 325.11 | 4912.10 | 742.16 |
| 325.11 | 5330.40 | 742.65 |
| 325.11 | 5702.30 | 743.08 |
| 325.11 | 6069.10 | 743.56 |
| 325.11 | 6403.00 | 743.98 |
| 325.11 | 6776.10 | 744.45 |
| 325.11 | 7099.20 | 744.86 |
| 325.11 | 7495.70 | 745.33 |
| 325.11 | 7840.20 | 745.77 |
| 325.11 | 8217.30 | 746.22 |
| 325.11 | 8572.10 | 746.68 |
| 325.11 | 8934.60 | 747.14 |
| 325.11 | 9271.10 | 747.56 |
| 325.11 | 9620.80 | 747.98 |
| 325.11 | 10045.40 | 748.47 |
| 345.10 | 2298.40 | 718.81 |
| 345.10 | 2347.50 | 718.97 |
| 345.10 | 2730.70 | 719.58 |
| 345.10 | 2993.90 | 720.06 |
| 345.10 | 3284.20 | 720.53 |
| 345.10 | 3545.40 | 720.93 |
| 345.10 | 3953.70 | 721.63 |
| 345.10 | 4112.50 | 721.93 |
| 345.10 | 4426.00 | 722.46 |
| 345.10 | 4706.40 | 722.89 |
| 345.10 | 5000.90 | 723.31 |
| 345.10 | 5282.10 | 723.84 |
| 345.10 | 5590.20 | 724.3 |
| 345.10 | 5944.60 | 724.83 |
| 345.10 | 6183.30 | 725.19 |
| 345.10 | 6485.90 | 725.68 |
| 345.10 | 6790.40 | 726.18 |
| 345.10 | 7088.30 | 726.63 |
| 345.10 | 7396.10 | 727.11 |
| 345.10 | 7697.50 | 727.55 |
| 345.10 | 8010.40 | 728.03 |
| 345.10 | 8324.50 | 728.51 |
| 345.10 | 8635.00 | 728.98 |
| 345.10 | 8947.20 | 729.42 |
| 345.10 | 9276.00 | 729.9 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.3031 (Liquid)
- Mole fraction = 0.5024 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 300.10 | 930.90 | 707.92 |
| 300.10 | 1197.00 | 708.29 |
| 300.10 | 1556.10 | 708.78 |
| 300.10 | 1948.10 | 709.29 |
| 300.10 | 2458.80 | 709.93 |
| 300.10 | 2780.10 | 710.37 |
| 300.10 | 3164.50 | 710.88 |
| 300.10 | 3512.80 | 711.35 |
| 300.10 | 4009.00 | 711.99 |
| 300.10 | 4360.40 | 712.44 |
| 300.10 | 4766.30 | 712.95 |
| 300.10 | 5154.60 | 713.45 |
| 300.10 | 5580.50 | 713.98 |
| 300.10 | 5973.40 | 714.47 |
| 300.10 | 6437.40 | 715.04 |
| 300.10 | 6813.90 | 715.51 |
| 300.10 | 7245.70 | 716.02 |
| 300.10 | 7676.20 | 716.54 |
| 300.10 | 8095.30 | 717.04 |
| 300.10 | 8527.10 | 717.54 |
| 300.10 | 9025.90 | 718.13 |
| 300.10 | 9429.00 | 718.61 |
| 300.10 | 9785.50 | 719.09 |
| 300.10 | 10213.80 | 719.6 |
| 325.13 | 1187.00 | 678.16 |
| 325.13 | 1443.20 | 678.62 |
| 325.13 | 1727.80 | 679.11 |
| 325.13 | 2143.60 | 679.8 |
| 325.13 | 2479.70 | 680.35 |
| 325.13 | 2891.40 | 681.1 |
| 325.13 | 3154.40 | 681.59 |
| 325.13 | 3531.80 | 682.22 |
| 325.13 | 3834.40 | 682.74 |
| 325.13 | 4104.10 | 683.18 |
| 325.13 | 4552.90 | 683.87 |
| 325.13 | 4913.70 | 684.44 |
| 325.13 | 5291.60 | 685.03 |
| 325.13 | 5673.00 | 685.61 |
| 325.13 | 6031.10 | 686.15 |
| 325.13 | 6401.70 | 686.72 |
| 325.13 | 6789.20 | 687.28 |
| 325.13 | 7173.60 | 687.86 |
| 325.13 | 7569.00 | 688.43 |
| 325.13 | 7965.20 | 689.02 |
| 325.13 | 8355.00 | 689.57 |
| 325.13 | 8763.70 | 690.16 |
| 325.13 | 9170.70 | 690.73 |
| 325.13 | 9574.80 | 691.28 |
| 325.13 | 9969.40 | 691.84 |
| 350.13 | 2436.80 | 653.52 |
| 350.13 | 2604.80 | 653.96 |
| 350.13 | 2930.10 | 654.68 |
| 350.13 | 3202.50 | 655.27 |
| 350.13 | 3734.40 | 656.44 |
| 350.13 | 3872.40 | 656.79 |
| 350.13 | 4136.90 | 657.4 |
| 350.13 | 4488.90 | 658.17 |
| 350.13 | 4810.50 | 658.86 |
| 350.13 | 5126.00 | 659.5 |
| 350.13 | 5445.20 | 660.17 |
| 350.13 | 5766.20 | 660.85 |
| 350.13 | 6092.80 | 661.51 |
| 350.13 | 6419.00 | 662.19 |
| 350.13 | 6762.00 | 662.87 |
| 350.13 | 7090.70 | 663.5 |
| 350.13 | 7423.40 | 664.19 |
| 350.13 | 7773.10 | 664.87 |
| 350.13 | 8125.80 | 665.54 |
| 350.13 | 8476.00 | 666.19 |
| 350.13 | 8829.50 | 666.84 |
| 350.13 | 9190.50 | 667.56 |
| 350.13 | 9544.70 | 668.2 |
| 350.13 | 9902.40 | 668.83 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.3906 (Liquid)
- Mole fraction = 0.4236 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 300.10 | 1018.70 | 680.98 |
| 300.10 | 1199.80 | 681.27 |
| 300.10 | 1620.90 | 681.88 |
| 300.10 | 1977.30 | 682.39 |
| 300.10 | 2327.90 | 682.91 |
| 300.10 | 2703.90 | 683.48 |
| 300.10 | 3029.60 | 683.95 |
| 300.10 | 3363.30 | 684.43 |
| 300.10 | 3758.10 | 685.0 |
| 300.10 | 4032.30 | 685.37 |
| 300.10 | 4487.20 | 686.01 |
| 300.10 | 4841.40 | 686.51 |
| 300.10 | 5211.20 | 687.02 |
| 300.10 | 5591.90 | 687.54 |
| 300.10 | 5957.50 | 688.05 |
| 300.10 | 6330.70 | 688.56 |
| 300.10 | 6708.40 | 689.06 |
| 300.10 | 7081.10 | 689.56 |
| 300.10 | 7464.90 | 690.07 |
| 300.10 | 7865.50 | 690.59 |
| 300.10 | 8251.90 | 691.1 |
| 300.10 | 8631.30 | 691.6 |
| 300.10 | 9014.00 | 692.09 |
| 300.10 | 9422.90 | 692.6 |
| 300.10 | 9832.40 | 693.12 |
| 325.11 | 1951.80 | 650.66 |
| 325.11 | 2356.10 | 651.45 |
| 325.11 | 2596.00 | 651.95 |
| 325.11 | 2934.10 | 652.61 |
| 325.11 | 3207.70 | 653.19 |
| 325.11 | 3493.80 | 653.75 |
| 325.11 | 3878.70 | 654.46 |
| 325.11 | 4223.40 | 655.08 |
| 325.11 | 4567.90 | 655.73 |
| 325.11 | 4892.60 | 656.32 |
| 325.11 | 5223.50 | 656.91 |
| 325.11 | 5558.60 | 657.52 |
| 325.11 | 5927.30 | 658.17 |
| 325.11 | 6278.00 | 658.79 |
| 325.11 | 6659.60 | 659.45 |
| 325.11 | 7005.10 | 660.05 |
| 325.11 | 7364.50 | 660.65 |
| 325.11 | 7730.70 | 661.26 |
| 325.11 | 8119.20 | 661.9 |
| 325.11 | 8474.30 | 662.48 |
| 325.11 | 8857.20 | 663.1 |
| 325.11 | 9233.60 | 663.72 |
| 325.11 | 9619.20 | 664.33 |
| 325.11 | 9971.40 | 664.93 |
| 350.11 | 2620.50 | 618.74 |
| 350.11 | 3007.20 | 619.87 |
| 350.11 | 3183.00 | 620.39 |
| 350.11 | 3528.10 | 621.38 |
| 350.11 | 3731.20 | 621.97 |
| 350.11 | 4088.40 | 622.82 |
| 350.11 | 4364.50 | 623.63 |
| 350.11 | 4653.60 | 624.39 |
| 350.11 | 4951.20 | 625.19 |
| 350.11 | 5258.20 | 625.98 |
| 350.11 | 5596.80 | 626.78 |
| 350.11 | 5945.80 | 627.64 |
| 350.11 | 6238.20 | 628.34 |
| 350.11 | 6568.00 | 629.17 |
| 350.11 | 6882.80 | 629.92 |
| 350.11 | 7201.80 | 630.66 |
| 350.11 | 7561.10 | 631.49 |
| 350.11 | 7908.70 | 632.29 |
| 350.11 | 8235.70 | 633.07 |
| 350.11 | 8584.70 | 633.86 |
| 350.11 | 8912.60 | 634.62 |
| 350.11 | 9291.10 | 635.35 |
| 350.11 | 9665.90 | 636.22 |
| 350.11 | 9987.40 | 636.95 |
Mass density, kg/m3 [ref]
Operational conditions:
- Mole fraction = 0.6123 (Liquid)
- Mole fraction = 0.3039 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 300.10 | 1085.40 | 614.94 |
| 300.10 | 1531.40 | 615.81 |
| 300.10 | 1870.70 | 616.53 |
| 300.10 | 2372.60 | 617.48 |
| 300.10 | 2527.20 | 617.84 |
| 300.10 | 2922.10 | 618.61 |
| 300.10 | 3226.20 | 619.19 |
| 300.10 | 3579.40 | 619.86 |
| 300.10 | 4068.20 | 620.74 |
| 300.10 | 4281.70 | 621.17 |
| 300.10 | 4729.00 | 622.0 |
| 300.10 | 5109.50 | 622.68 |
| 300.10 | 5494.50 | 623.39 |
| 300.10 | 5875.10 | 624.07 |
| 300.10 | 6252.10 | 624.73 |
| 300.10 | 6636.50 | 625.4 |
| 300.10 | 7032.90 | 626.07 |
| 300.10 | 7453.40 | 626.76 |
| 300.10 | 7866.20 | 627.47 |
| 300.10 | 8255.70 | 628.11 |
| 300.10 | 8661.90 | 628.75 |
| 300.10 | 9079.60 | 629.46 |
| 300.10 | 9474.20 | 630.08 |
| 300.10 | 9896.70 | 630.79 |
| 325.12 | 1894.10 | 580.11 |
| 325.12 | 2207.30 | 580.96 |
| 325.12 | 2528.10 | 581.84 |
| 325.12 | 2847.40 | 582.67 |
| 325.12 | 3200.80 | 583.61 |
| 325.12 | 3499.10 | 584.39 |
| 325.12 | 3778.00 | 585.12 |
| 325.12 | 3817.50 | 586.14 |
| 325.12 | 4214.20 | 587.19 |
| 325.12 | 4522.10 | 587.93 |
| 325.12 | 4866.30 | 588.81 |
| 325.12 | 5210.20 | 589.63 |
| 325.12 | 5562.90 | 590.47 |
| 325.12 | 5930.30 | 591.32 |
| 325.12 | 6321.20 | 592.2 |
| 325.12 | 6686.30 | 593.02 |
| 325.12 | 7057.50 | 593.82 |
| 325.12 | 7468.80 | 594.69 |
| 325.12 | 7876.20 | 595.54 |
| 325.12 | 8253.60 | 596.34 |
| 325.12 | 8653.20 | 597.15 |
| 325.12 | 9078.40 | 597.99 |
| 325.12 | 9500.10 | 598.83 |
| 325.12 | 9915.50 | 599.65 |
| 350.10 | 2850.10 | 540.02 |
| 350.10 | 3016.80 | 540.87 |
| 350.10 | 3231.50 | 541.94 |
| 350.10 | 3505.70 | 543.11 |
| 350.10 | 3782.70 | 544.27 |
| 350.10 | 3996.50 | 545.27 |
| 350.10 | 4328.10 | 546.57 |
| 350.10 | 4621.10 | 547.8 |
| 350.10 | 4866.70 | 548.79 |
| 350.10 | 5169.30 | 550.07 |
| 350.10 | 5457.30 | 551.09 |
| 350.10 | 5759.20 | 552.24 |
| 350.10 | 6094.30 | 553.32 |
| 350.10 | 6419.10 | 554.43 |
| 350.10 | 6732.10 | 555.54 |
| 350.10 | 7048.00 | 556.69 |
| 350.10 | 7372.90 | 557.82 |
| 350.10 | 7703.00 | 558.93 |
| 350.10 | 8059.80 | 559.96 |
| 350.10 | 8438.50 | 561.12 |
| 350.10 | 8820.80 | 562.37 |
| 350.10 | 9187.70 | 563.44 |
| 350.10 | 9575.50 | 564.54 |
| 350.10 | 9939.10 | 565.57 |