- Name
- Carbonic acid, dimethyl ester
- InChI
- InChI=1S/C3H6O3/c1-5-3(4)6-2/h1-2H3
- InChI Key
- IEJIGPNLZYLLBP-UHFFFAOYSA-N
- Formula
- C3H6O3
- SMILES
- COC(=O)OC
- Mol. Weight (g/mol)
- 90.08
- CAS
- 616-38-6
- Name
- Ethylbenzene
- InChI
- InChI=1S/C8H10/c1-2-8-6-4-3-5-7-8/h3-7H,2H2,1H3
- InChI Key
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N
- Formula
- C8H10
- SMILES
- CCc1ccccc1
- Mol. Weight (g/mol)
- 106.17
- CAS
- 100-41-4
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 (2)
- Excess molar enthalpy (molar enthalpy (4)
- n0 - Refractive index (Na D-line) (2)
- Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of Ethylbenzene (2) [ref]
Operational condition: Pressure, kPa = 93.13 (Gas)
| Mole fraction of Ethylbenzene (2) - Liquid | Mole fraction of Ethylbenzene (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0393 | 0.0219 |
| 0.0622 | 0.0330 |
| 0.1590 | 0.0693 |
| 0.2804 | 0.1104 |
| 0.3954 | 0.1475 |
| 0.4778 | 0.1782 |
| 0.6295 | 0.2524 |
| 0.7054 | 0.3081 |
| 0.8066 | 0.4176 |
| 0.8897 | 0.5730 |
| 0.9303 | 0.6839 |
| 1.0000 | 1.0000 |
Mole fraction of Ethylbenzene (2)
Mole fraction of Ethylbenzene (2)
0
0.2
0.4
0.6
0.8
1
0
0.5
1
Mole fraction of Ethylbenzene (2) [ref]
Operational condition: Pressure, kPa = 93.13 (Gas)
| Mole fraction of Ethylbenzene (2) - Liquid | Mole fraction of Ethylbenzene (2) - Gas |
|---|---|
| 0.0000 | 0.0000 |
| 0.0393 | 0.0219 |
| 0.0622 | 0.0330 |
| 0.1590 | 0.0693 |
| 0.2804 | 0.1104 |
| 0.3954 | 0.1475 |
| 0.4778 | 0.1782 |
| 0.6295 | 0.2524 |
| 0.7054 | 0.3081 |
| 0.8066 | 0.4176 |
| 0.8897 | 0.5730 |
| 0.9303 | 0.6839 |
| 1.0000 | 1.0000 |
Mole fraction of Ethylbenzene (2)
Mole fraction of Ethylbenzene (2)
0
0.2
0.4
0.6
0.8
1
0
0.5
1
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0501 | 0.0899 |
| 0.1003 | 0.2048 |
| 0.1490 | 0.2674 |
| 0.2010 | 0.3548 |
| 0.2512 | 0.4344 |
| 0.2998 | 0.4993 |
| 0.3525 | 0.5570 |
| 0.4005 | 0.5997 |
| 0.4524 | 0.6289 |
| 0.5025 | 0.6418 |
| 0.5507 | 0.6416 |
| 0.6020 | 0.6297 |
| 0.6513 | 0.6054 |
| 0.7011 | 0.5651 |
| 0.7512 | 0.5131 |
| 0.8012 | 0.4455 |
| 0.8513 | 0.3620 |
| 0.9012 | 0.2607 |
| 0.9509 | 0.1403 |
Mole fraction of Carbonic acid, dimethyl ester (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.1
0.2
0.3
0.4
0.5
0.6
0.2
0.4
0.6000000000000001
0.8
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 10200 (Liquid)
| Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0501 | 0.1008 |
| 0.1004 | 0.2125 |
| 0.1491 | 0.2681 |
| 0.2011 | 0.3616 |
| 0.2514 | 0.4460 |
| 0.3000 | 0.5125 |
| 0.3528 | 0.5719 |
| 0.4009 | 0.6116 |
| 0.4528 | 0.6383 |
| 0.5028 | 0.6525 |
| 0.5510 | 0.6516 |
| 0.6023 | 0.6361 |
| 0.6517 | 0.6087 |
| 0.7014 | 0.5698 |
| 0.7514 | 0.5180 |
| 0.8014 | 0.4488 |
| 0.8514 | 0.3669 |
| 0.9013 | 0.2706 |
| 0.9508 | 0.1460 |
Mole fraction of Carbonic acid, dimethyl ester (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.2
0.4
0.6000000000000001
0.8
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Pressure, kPa = 101.3 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0501 | 0.0899 |
| 0.1003 | 0.2048 |
| 0.1490 | 0.2674 |
| 0.2010 | 0.3548 |
| 0.2512 | 0.4344 |
| 0.2998 | 0.4993 |
| 0.3525 | 0.5570 |
| 0.4005 | 0.5997 |
| 0.4524 | 0.6289 |
| 0.5025 | 0.6418 |
| 0.5507 | 0.6416 |
| 0.6020 | 0.6297 |
| 0.6513 | 0.6054 |
| 0.7011 | 0.5651 |
| 0.7512 | 0.5131 |
| 0.8012 | 0.4455 |
| 0.8513 | 0.3620 |
| 0.9012 | 0.2607 |
| 0.9509 | 0.1403 |
Mole fraction of Carbonic acid, dimethyl ester (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.1
0.2
0.3
0.4
0.5
0.6
0.2
0.4
0.6000000000000001
0.8
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 10200 (Liquid)
| Mole fraction of Carbonic acid, dimethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0501 | 0.1008 |
| 0.1004 | 0.2125 |
| 0.1491 | 0.2681 |
| 0.2011 | 0.3616 |
| 0.2514 | 0.4460 |
| 0.3000 | 0.5125 |
| 0.3528 | 0.5719 |
| 0.4009 | 0.6116 |
| 0.4528 | 0.6383 |
| 0.5028 | 0.6525 |
| 0.5510 | 0.6516 |
| 0.6023 | 0.6361 |
| 0.6517 | 0.6087 |
| 0.7014 | 0.5698 |
| 0.7514 | 0.5180 |
| 0.8014 | 0.4488 |
| 0.8514 | 0.3669 |
| 0.9013 | 0.2706 |
| 0.9508 | 0.1460 |
Mole fraction of Carbonic acid, dimethyl ester (1)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.2
0.4
0.6000000000000001
0.8
Refractive index (Na D-line) [ref]
Operational conditions:
- Pressure, kPa = 93 (Liquid)
- Temperature, K = 293.15 (Liquid)
| Mole fraction of Ethylbenzene (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0000 | 1.3688 |
| 0.0462 | 1.3767 |
| 0.0890 | 1.3836 |
| 0.1753 | 1.397 |
| 0.2701 | 1.4109 |
| 0.3564 | 1.4232 |
| 0.4359 | 1.4335 |
| 0.4448 | 1.4352 |
| 0.4680 | 1.4382 |
| 0.5157 | 1.4441 |
| 0.5825 | 1.4527 |
| 0.6639 | 1.4617 |
| 0.7377 | 1.4702 |
| 0.8520 | 1.4815 |
| 0.8827 | 1.4847 |
| 0.9124 | 1.4873 |
| 0.9395 | 1.49 |
| 1.0000 | 1.4956 |
Mole fraction of Ethylbenzene (2)
Refractive index (Na D-line)
1.36
1.38
1.4
1.42
1.44
1.46
1.48
1.5
0
0.5
1
Refractive index (Na D-line) [ref]
Operational conditions:
- Pressure, kPa = 93 (Liquid)
- Temperature, K = 293.15 (Liquid)
| Mole fraction of Ethylbenzene (2) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0000 | 1.3688 |
| 0.0462 | 1.3767 |
| 0.0890 | 1.3836 |
| 0.1753 | 1.397 |
| 0.2701 | 1.4109 |
| 0.3564 | 1.4232 |
| 0.4359 | 1.4335 |
| 0.4448 | 1.4352 |
| 0.4680 | 1.4382 |
| 0.5157 | 1.4441 |
| 0.5825 | 1.4527 |
| 0.6639 | 1.4617 |
| 0.7377 | 1.4702 |
| 0.8520 | 1.4815 |
| 0.8827 | 1.4847 |
| 0.9124 | 1.4873 |
| 0.9395 | 1.49 |
| 1.0000 | 1.4956 |
Mole fraction of Ethylbenzene (2)
Refractive index (Na D-line)
1.36
1.38
1.4
1.42
1.44
1.46
1.48
1.5
0
0.5
1
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 93.13 (Gas)
| Mole fraction of Ethylbenzene (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 360.73 |
| 0.0393 | 361.24 |
| 0.0622 | 361.55 |
| 0.1590 | 362.91 |
| 0.2804 | 364.85 |
| 0.3954 | 367.04 |
| 0.4778 | 368.97 |
| 0.6295 | 373.77 |
| 0.7054 | 377.14 |
| 0.8066 | 383.26 |
| 0.8897 | 390.65 |
| 0.9303 | 395.26 |
| 1.0000 | 406.23 |
Mole fraction of Ethylbenzene (2)
Boiling temperature at pressure P, K
360
370
380
390
400
410
0
0.5
1
Boiling temperature at pressure P, K [ref]
Operational condition: Pressure, kPa = 93.13 (Gas)
| Mole fraction of Ethylbenzene (2) - Liquid | Boiling temperature at pressure P, K - Liquid |
|---|---|
| 0.0000 | 360.73 |
| 0.0393 | 361.24 |
| 0.0622 | 361.55 |
| 0.1590 | 362.91 |
| 0.2804 | 364.85 |
| 0.3954 | 367.04 |
| 0.4778 | 368.97 |
| 0.6295 | 373.77 |
| 0.7054 | 377.14 |
| 0.8066 | 383.26 |
| 0.8897 | 390.65 |
| 0.9303 | 395.26 |
| 1.0000 | 406.23 |
Mole fraction of Ethylbenzene (2)
Boiling temperature at pressure P, K
360
370
380
390
400
410
0
0.5
1
Sources
- Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
- Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
- Excess Molar Enthalpies for Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene or Ethyl Benzoate at 298.15 K and 10.2 MPa