- InChI
- InChI=1S/C3H6O3/c1-5-3(4)6-2/h1-2H3
- InChI Key
- IEJIGPNLZYLLBP-UHFFFAOYSA-N
- Formula
- C3H6O3
- SMILES
- COC(=O)OC
- Molecular Weight1
- 90.08
- CAS
- 616-38-6
- Other Names
-
- CH3OCOOCH3
- Dimethyl carbonate
- Dimethyl ester of carbonic acid
- Methyl carbonate
- Methyl carbonate ((MeO)2CO)
- UN 1161
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 830.20 | kJ/mol | NIST |
| BasG | 799.20 | kJ/mol | NIST |
| ΔfG° | -364.54 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -482.27 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 7.50 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [37.70; 38.00] | kJ/mol |
|
| ΔvapH° | 38.00 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 37.70 ± 0.20 | kJ/mol | NIST |
| IE | [11.00; 11.20] | eV |
|
| IE | 11.00 | eV | NIST |
| IE | 11.20 | eV | NIST |
| IE | 11.00 | eV | NIST |
| log10WS | -5.89e-03 | Crippen Calculated Property | |
| logPoct/wat | 0.399 | Crippen Calculated Property | |
| McVol | 66.440 | ml/mol | McGowan Calculated Property |
| Pc | [4800.00; 4800.00] | kPa |
|
| Pc | 4800.00 ± 150.00 | kPa | NIST |
| Pc | 4800.00 ± 300.00 | kPa | NIST |
| ρc | [342.30; 357.61] | kg/m3 |
|
| ρc | 357.61 ± 9.91 | kg/m3 | NIST |
| ρc | 342.30 ± 15.31 | kg/m3 | NIST |
| Inp | 620.00 | NIST | |
| Tboil | [337.84; 363.70] | K |
|
| Tboil | 363.46 | K | VLE of ... |
| Tboil | Outlier 337.84 | K | Measure... |
| Tboil | 363.35 | K | Vapour-... |
| Tboil | 363.36 | K | Measure... |
| Tboil | 363.46 | K | Densiti... |
| Tboil | 363.46 | K | Measure... |
| Tboil | 363.25 | K | Isobari... |
| Tboil | 363.41 | K | Organic... |
| Tboil | 363.60 ± 0.10 | K | NIST |
| Tboil | 363.70 | K | NIST |
| Tboil | 363.00 | K | NIST |
| Tboil | 363.60 ± 0.40 | K | NIST |
| Tboil | 363.60 ± 0.30 | K | NIST |
| Tboil | 363.40 ± 0.40 | K | NIST |
| Tboil | 363.50 ± 0.50 | K | NIST |
| Tboil | 363.50 ± 0.50 | K | NIST |
| Tboil | 363.50 ± 0.50 | K | NIST |
| Tc | [557.00; 557.00] | K |
|
| Tc | 557.00 ± 2.00 | K | NIST |
| Tc | 557.00 ± 2.00 | K | NIST |
| Tfus | [267.55; 278.20] | K |
|
| Tfus | 278.16 | K | Solid-l... |
| Tfus | 278.20 | K | The sol... |
| Tfus | 277.06 | K | Efficie... |
| Tfus | 277.57 | K | Vapor P... |
| Tfus | 278.16 | K | Solid-L... |
| Tfus | Outlier 267.55 ± 0.50 | K | NIST |
| Vc | 0.245 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [116.81; 146.98] | J/mol×K | [366.75; 547.10] |
|
| Cp,gas | 116.81 | J/mol×K | 366.75 | Joback Calculated Property |
| Cp,gas | 121.94 | J/mol×K | 396.81 | Joback Calculated Property |
| Cp,gas | 127.04 | J/mol×K | 426.87 | Joback Calculated Property |
| Cp,gas | 132.12 | J/mol×K | 456.93 | Joback Calculated Property |
| Cp,gas | 137.14 | J/mol×K | 486.99 | Joback Calculated Property |
| Cp,gas | 142.10 | J/mol×K | 517.05 | Joback Calculated Property |
| Cp,gas | 146.98 | J/mol×K | 547.10 | Joback Calculated Property |
| Cp,liquid | [153.20; 173.68] | J/mol×K | [288.15; 333.15] |
|
| Cp,liquid | 153.20 | J/mol×K | 288.15 | Excess ... |
| Cp,liquid | 165.51 | J/mol×K | 288.15 | Densiti... |
| Cp,liquid | 164.03 | J/mol×K | 288.15 | Thermod... |
| Cp,liquid | 163.61 | J/mol×K | 288.15 | Isobari... |
| Cp,liquid | 156.10 | J/mol×K | 293.15 | Excess ... |
| Cp,liquid | 166.07 | J/mol×K | 293.15 | Densiti... |
| Cp,liquid | 165.02 | J/mol×K | 298.15 | Thermod... |
| Cp,liquid | 164.65 | J/mol×K | 298.15 | Isobari... |
| Cp,liquid | 157.90 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 167.10 | J/mol×K | 298.15 | Densiti... |
| Cp,liquid | 159.80 | J/mol×K | 303.15 | Excess ... |
| Cp,liquid | 168.48 | J/mol×K | 303.15 | Densiti... |
| Cp,liquid | 161.70 | J/mol×K | 308.15 | Excess ... |
| Cp,liquid | 166.30 | J/mol×K | 308.15 | Thermod... |
| Cp,liquid | 169.72 | J/mol×K | 308.15 | Densiti... |
| Cp,liquid | 165.92 | J/mol×K | 308.15 | Isobari... |
| Cp,liquid | 170.83 | J/mol×K | 313.15 | Densiti... |
| Cp,liquid | 162.90 | J/mol×K | 313.15 | Excess ... |
| Cp,liquid | 163.00 | J/mol×K | 318.15 | Excess ... |
| Cp,liquid | 172.18 | J/mol×K | 318.15 | Densiti... |
| Cp,liquid | 163.60 | J/mol×K | 323.15 | Excess ... |
| Cp,liquid | 173.68 | J/mol×K | 323.15 | Densiti... |
| Cp,liquid | 163.80 | J/mol×K | 328.15 | Excess ... |
| Cp,liquid | 164.80 | J/mol×K | 333.15 | Excess ... |
| η | [0.0003527; 0.0006230] | Pa×s | [293.15; 343.15] |
|
| η | 0.0006230 | Pa×s | 293.15 | Dynamic... |
| η | 0.0006230 | Pa×s | 293.15 | Density... |
| η | 0.0006163 | Pa×s | 293.15 | Excess ... |
| η | 0.0006173 | Pa×s | 293.15 | Excess ... |
| η | 0.0005771 | Pa×s | 298.15 | Excess ... |
| η | 0.0005840 | Pa×s | 298.15 | Dynamic... |
| η | 0.0005734 | Pa×s | 298.15 | Excess ... |
| η | 0.0005840 | Pa×s | 298.15 | Density... |
| η | 0.0005490 | Pa×s | 303.15 | Density... |
| η | 0.0005403 | Pa×s | 303.15 | Excess ... |
| η | 0.0005490 | Pa×s | 303.15 | Dynamic... |
| η | 0.0005433 | Pa×s | 303.15 | Excess ... |
| η | 0.0005170 | Pa×s | 308.15 | Density... |
| η | 0.0004807 | Pa×s | 313.15 | Excess ... |
| η | 0.0004880 | Pa×s | 313.15 | Dynamic... |
| η | 0.0004820 | Pa×s | 313.15 | Excess ... |
| η | 0.0004880 | Pa×s | 313.15 | Density... |
| η | 0.0004270 | Pa×s | 323.15 | Excess ... |
| η | 0.0004319 | Pa×s | 323.15 | Excess ... |
| η | 0.0003893 | Pa×s | 333.15 | Excess ... |
| η | 0.0003527 | Pa×s | 343.15 | Excess ... |
| ΔfusH | 11.58 | kJ/mol | 278.20 | NIST |
| ΔvapH | 36.40 | kJ/mol | 368.50 | NIST |
| Pvap | [1.92; 566.47] | kPa | [274.20; 428.15] |
|
| Pvap | 1.92 | kPa | 274.20 | Vapour ... |
| Pvap | 1.98 | kPa | 275.00 | Vapour ... |
| Pvap | 2.14 | kPa | 276.00 | Vapour ... |
| Pvap | 2.28 | kPa | 276.90 | Vapour ... |
| Pvap | 2.43 | kPa | 277.90 | Vapour ... |
| Pvap | 2.30 | kPa | 277.96 | Low pre... |
| Pvap | 2.84 | kPa | 280.70 | Vapour ... |
| Pvap | 3.12 | kPa | 282.06 | Low pre... |
| Pvap | 3.27 | kPa | 283.20 | Vapour ... |
| Pvap | 3.85 | kPa | 285.80 | Vapour ... |
| Pvap | 4.02 | kPa | 286.15 | Low pre... |
| Pvap | 4.42 | kPa | 288.20 | Vapour ... |
| Pvap | 4.86 | kPa | 290.25 | Low pre... |
| Pvap | 4.98 | kPa | 290.80 | Vapour ... |
| Pvap | 10.00 | kPa | 293.00 | Vapor-L... |
| Pvap | 5.71 | kPa | 293.10 | Vapour ... |
| Pvap | 6.31 | kPa | 294.35 | Low pre... |
| Pvap | 6.72 | kPa | 295.70 | Vapour ... |
| Pvap | 6.98 | kPa | 298.15 | Low pre... |
| Pvap | 7.57 | kPa | 298.30 | Vapour ... |
| Pvap | 8.55 | kPa | 300.70 | Vapour ... |
| Pvap | 9.72 | kPa | 302.54 | Low pre... |
| Pvap | 9.68 | kPa | 303.20 | Vapour ... |
| Pvap | 9.98 | kPa | 304.10 | Vapour ... |
| Pvap | 11.70 | kPa | 306.64 | Low pre... |
| Pvap | 14.02 | kPa | 310.74 | Low pre... |
| Pvap | 20.00 | kPa | 313.00 | Vapor-L... |
| Pvap | 19.82 | kPa | 318.15 | Low pre... |
| Pvap | 23.07 | kPa | 323.15 | Low pre... |
| Pvap | 41.02 | kPa | 337.35 | Measure... |
| Pvap | 70.00 | kPa | 353.00 | Vapor-L... |
| Pvap | 101.32 | kPa | 363.25 | Isobari... |
| Pvap | 101.30 | kPa | 363.35 | Vapour-... |
| Pvap | 101.30 | kPa | 363.36 | Measure... |
| Pvap | 101.32 | kPa | 363.41 | Organic... |
| Pvap | 140.00 | kPa | 373.00 | Vapor-L... |
| Pvap | 154.63 | kPa | 377.15 | Measure... |
| Pvap | 229.39 | kPa | 391.15 | Measure... |
| Pvap | 382.50 | kPa | 411.15 | Measure... |
| Pvap | 566.47 | kPa | 428.15 | Measure... |
| n0 | [1.35370; 1.36720] | [298.15; 298.15] |
|
|
| n0 | 1.36720 | 298.15 | Liquid ... | |
| n0 | 1.36654 | 298.15 | Isother... | |
| n0 | 1.36654 | 298.15 | Isother... | |
| n0 | 1.36640 | 298.15 | Propert... | |
| n0 | 1.36640 | 298.15 | Vapor-L... | |
| n0 | 1.36640 | 298.15 | Isobari... | |
| n0 | 1.35370 | 298.15 | Bubble ... | |
| n0 | 1.36600 | 298.15 | Viscosi... | |
| n0 | 1.36647 | 298.15 | Isother... | |
| ρl | [1016.32; 1076.43] | kg/m3 | [288.15; 333.15] |
|
| ρl | 1076.43 | kg/m3 | 288.15 | Permitt... |
| ρl | 1076.39 | kg/m3 | 288.15 | Excess ... |
| ρl | 1069.86 | kg/m3 | 293.15 | Excess ... |
| ρl | 1069.83 | kg/m3 | 293.15 | Volumet... |
| ρl | 1069.80 | kg/m3 | 293.15 | Densiti... |
| ρl | 1069.92 | kg/m3 | 293.15 | Density... |
| ρl | 1069.60 | kg/m3 | 293.15 | Densiti... |
| ρl | 1069.70 | kg/m3 | 293.15 | Density... |
| ρl | 1069.95 | kg/m3 | 293.15 | Permitt... |
| ρl | 1069.79 | kg/m3 | 293.15 | Density... |
| ρl | 1063.10 | kg/m3 | 298.15 | Excess ... |
| ρl | 1063.40 | kg/m3 | 298.15 | Vapor p... |
| ρl | 1063.26 | kg/m3 | 298.15 | Liquid ... |
| ρl | 1063.38 | kg/m3 | 298.15 | Ebullio... |
| ρl | 1063.26 | kg/m3 | 298.15 | Permitt... |
| ρl | 1062.80 | kg/m3 | 298.15 | Densiti... |
| ρl | 1063.34 | kg/m3 | 298.15 | Density... |
| ρl | 1070.00 | kg/m3 | 298.15 | Low pre... |
| ρl | 1063.24 | kg/m3 | 298.15 | Isother... |
| ρl | 1063.26 | kg/m3 | 298.15 | Solid-l... |
| ρl | 1060.87 | kg/m3 | 298.15 | Solid-l... |
| ρl | 1063.20 | kg/m3 | 298.15 | Densiti... |
| ρl | 1063.30 | kg/m3 | 298.15 | Isobari... |
| ρl | 1063.26 | kg/m3 | 298.15 | Ternary... |
| ρl | 1063.25 | kg/m3 | 298.15 | Volumet... |
| ρl | 1063.10 | kg/m3 | 298.15 | Excess ... |
| ρl | 1063.19 | kg/m3 | 298.15 | Measure... |
| ρl | 1062.97 | kg/m3 | 298.15 | Densiti... |
| ρl | 1063.50 | kg/m3 | 298.15 | Viscosi... |
| ρl | 1063.35 | kg/m3 | 298.15 | Excess ... |
| ρl | 1063.26 | kg/m3 | 298.15 | Isobari... |
| ρl | 1063.10 | kg/m3 | 298.15 | Density... |
| ρl | 1063.29 | kg/m3 | 298.15 | Separat... |
| ρl | 1063.27 | kg/m3 | 298.15 | Excess ... |
| ρl | 1061.90 | kg/m3 | 298.20 | Liquid ... |
| ρl | 1061.90 | kg/m3 | 298.20 | Liquid ... |
| ρl | 1056.40 | kg/m3 | 303.15 | Density... |
| ρl | 1056.50 | kg/m3 | 303.15 | Densiti... |
| ρl | 1056.80 | kg/m3 | 303.15 | Investi... |
| ρl | 1056.75 | kg/m3 | 303.15 | Density... |
| ρl | 1056.72 | kg/m3 | 303.15 | Density... |
| ρl | 1056.63 | kg/m3 | 303.15 | Volumet... |
| ρl | 1056.65 | kg/m3 | 303.15 | Excess ... |
| ρl | 1056.20 | kg/m3 | 303.15 | Densiti... |
| ρl | 1056.61 | kg/m3 | 303.15 | Permitt... |
| ρl | 1050.01 | kg/m3 | 308.15 | Permitt... |
| ρl | 1050.08 | kg/m3 | 308.15 | Volumet... |
| ρl | 1049.80 | kg/m3 | 308.15 | Densiti... |
| ρl | 1049.70 | kg/m3 | 308.15 | Density... |
| ρl | 1050.07 | kg/m3 | 308.15 | Density... |
| ρl | 1050.00 | kg/m3 | 308.15 | Excess ... |
| ρl | 1049.80 | kg/m3 | 308.15 | Densiti... |
| ρl | 1050.20 | kg/m3 | 308.15 | Investi... |
| ρl | 1043.37 | kg/m3 | 313.15 | Density... |
| ρl | 1043.00 | kg/m3 | 313.15 | Densiti... |
| ρl | 1043.29 | kg/m3 | 313.15 | Excess ... |
| ρl | 1043.10 | kg/m3 | 313.15 | Density... |
| ρl | 1043.39 | kg/m3 | 313.15 | Density... |
| ρl | 1043.19 | kg/m3 | 313.15 | Densiti... |
| ρl | 1043.50 | kg/m3 | 313.15 | Investi... |
| ρl | 1042.50 | kg/m3 | 313.15 | Densiti... |
| ρl | 1043.44 | kg/m3 | 313.15 | Volumet... |
| ρl | 1044.63 | kg/m3 | 313.15 | Densiti... |
| ρl | 1036.69 | kg/m3 | 318.15 | Density... |
| ρl | 1036.57 | kg/m3 | 318.15 | Excess ... |
| ρl | 1036.80 | kg/m3 | 318.15 | Investi... |
| ρl | 1036.62 | kg/m3 | 318.15 | Volumet... |
| ρl | 1036.40 | kg/m3 | 318.15 | Density... |
| ρl | 1035.60 | kg/m3 | 318.15 | Densiti... |
| ρl | 1036.65 | kg/m3 | 318.15 | Permitt... |
| ρl | 1029.83 | kg/m3 | 323.15 | Excess ... |
| ρl | 1030.00 | kg/m3 | 323.15 | Investi... |
| ρl | 1029.88 | kg/m3 | 323.15 | Volumet... |
| ρl | 1029.94 | kg/m3 | 323.15 | Density... |
| ρl | 1029.60 | kg/m3 | 323.15 | Density... |
| ρl | 1028.40 | kg/m3 | 323.15 | Densiti... |
| ρl | 1022.80 | kg/m3 | 328.15 | Density... |
| ρl | 1023.25 | kg/m3 | 328.15 | Density... |
| ρl | 1022.92 | kg/m3 | 328.15 | Permitt... |
| ρl | 1023.03 | kg/m3 | 328.15 | Excess ... |
| ρl | 1016.32 | kg/m3 | 333.15 | Density... |
| γ | [0.03; 0.03] | N/m | [298.15; 308.15] |
|
| γ | 0.03 | N/m | 298.15 | Analysi... |
| γ | 0.03 | N/m | 308.15 | Surface... |
Datasets
Refractive index (Na D-line)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 93.00 | 298.15 | 1.3664 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 1076.5 |
| 288.15 | 5000.00 | 1080.6 |
| 288.15 | 10000.00 | 1084.8 |
| 288.15 | 20000.00 | 1092.8 |
| 288.15 | 30000.00 | 1100.3 |
| 288.15 | 40000.00 | 1107.5 |
| 298.15 | 100.00 | 1062.9 |
| 298.15 | 5000.00 | 1068.0 |
| 298.15 | 10000.00 | 1072.1 |
| 298.15 | 20000.00 | 1080.5 |
| 298.15 | 30000.00 | 1088.5 |
| 298.15 | 40000.00 | 1095.9 |
| 308.15 | 100.00 | 1049.4 |
| 308.15 | 5000.00 | 1054.6 |
| 308.15 | 10000.00 | 1059.4 |
| 308.15 | 20000.00 | 1068.3 |
| 308.15 | 30000.00 | 1076.7 |
| 308.15 | 40000.00 | 1084.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 1076.83 |
| 288.15 | 5000.00 | 1081.15 |
| 288.15 | 10000.00 | 1085.32 |
| 288.15 | 15000.00 | 1089.52 |
| 288.15 | 20000.00 | 1093.35 |
| 288.15 | 25000.00 | 1096.99 |
| 288.15 | 30000.00 | 1100.63 |
| 288.15 | 35000.00 | 1104.08 |
| 288.15 | 40000.00 | 1107.4 |
| 293.15 | 100.00 | 1070.06 |
| 293.15 | 5000.00 | 1074.62 |
| 293.15 | 10000.00 | 1078.93 |
| 293.15 | 15000.00 | 1083.01 |
| 293.15 | 20000.00 | 1087.08 |
| 293.15 | 25000.00 | 1091.03 |
| 293.15 | 30000.00 | 1094.75 |
| 293.15 | 35000.00 | 1098.34 |
| 293.15 | 40000.00 | 1101.84 |
| 298.15 | 100.00 | 1063.45 |
| 298.15 | 5000.00 | 1068.0 |
| 298.15 | 10000.00 | 1072.51 |
| 298.15 | 15000.00 | 1076.72 |
| 298.15 | 20000.00 | 1080.9 |
| 298.15 | 25000.00 | 1084.89 |
| 298.15 | 30000.00 | 1088.82 |
| 298.15 | 35000.00 | 1092.44 |
| 298.15 | 40000.00 | 1096.04 |
| 303.15 | 100.00 | 1056.61 |
| 303.15 | 5000.00 | 1061.47 |
| 303.15 | 10000.00 | 1066.02 |
| 303.15 | 15000.00 | 1070.49 |
| 303.15 | 20000.00 | 1074.79 |
| 303.15 | 25000.00 | 1078.99 |
| 303.15 | 30000.00 | 1082.9 |
| 303.15 | 35000.00 | 1086.6 |
| 303.15 | 40000.00 | 1090.4 |
| 308.15 | 100.00 | 1049.91 |
| 308.15 | 5000.00 | 1054.84 |
| 308.15 | 10000.00 | 1059.69 |
| 308.15 | 15000.00 | 1064.3 |
| 308.15 | 20000.00 | 1068.73 |
| 308.15 | 25000.00 | 1073.0 |
| 308.15 | 30000.00 | 1077.1 |
| 308.15 | 35000.00 | 1080.78 |
| 308.15 | 40000.00 | 1084.38 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 1083.17 |
| 100.00 | 288.15 | 1076.43 |
| 100.00 | 293.15 | 1069.76 |
| 100.00 | 298.15 | 1063.1 |
| 100.00 | 303.15 | 1056.41 |
| 100.00 | 308.15 | 1049.66 |
| 100.00 | 313.15 | 1042.86 |
| 100.00 | 318.15 | 1036.04 |
| 100.00 | 323.15 | 1029.21 |
| 100.00 | 328.15 | 1022.24 |
| 5000.00 | 283.15 | 1087.33 |
| 5000.00 | 288.15 | 1080.8 |
| 5000.00 | 293.15 | 1074.22 |
| 5000.00 | 298.15 | 1067.7 |
| 5000.00 | 303.15 | 1061.17 |
| 5000.00 | 308.15 | 1054.59 |
| 5000.00 | 313.15 | 1047.94 |
| 5000.00 | 318.15 | 1041.3 |
| 5000.00 | 323.15 | 1034.63 |
| 5000.00 | 328.15 | 1027.92 |
| 10000.00 | 283.15 | 1091.39 |
| 10000.00 | 288.15 | 1085.02 |
| 10000.00 | 293.15 | 1078.58 |
| 10000.00 | 298.15 | 1072.21 |
| 10000.00 | 303.15 | 1065.82 |
| 10000.00 | 308.15 | 1059.39 |
| 10000.00 | 313.15 | 1052.91 |
| 10000.00 | 318.15 | 1046.44 |
| 10000.00 | 323.15 | 1039.95 |
| 10000.00 | 328.15 | 1033.45 |
| 15000.00 | 283.15 | 1095.34 |
| 15000.00 | 288.15 | 1089.07 |
| 15000.00 | 293.15 | 1082.76 |
| 15000.00 | 298.15 | 1076.52 |
| 15000.00 | 303.15 | 1070.29 |
| 15000.00 | 308.15 | 1064.0 |
| 15000.00 | 313.15 | 1057.67 |
| 15000.00 | 318.15 | 1051.36 |
| 15000.00 | 323.15 | 1045.04 |
| 15000.00 | 328.15 | 1038.69 |
| 20000.00 | 283.15 | 1099.13 |
| 20000.00 | 288.15 | 1093.0 |
| 20000.00 | 293.15 | 1086.83 |
| 20000.00 | 298.15 | 1080.7 |
| 20000.00 | 303.15 | 1074.59 |
| 20000.00 | 308.15 | 1068.43 |
| 20000.00 | 313.15 | 1062.22 |
| 20000.00 | 318.15 | 1056.08 |
| 20000.00 | 323.15 | 1049.91 |
| 20000.00 | 328.15 | 1043.71 |
| 25000.00 | 283.15 | 1102.79 |
| 25000.00 | 288.15 | 1096.79 |
| 25000.00 | 293.15 | 1090.73 |
| 25000.00 | 298.15 | 1084.74 |
| 25000.00 | 303.15 | 1078.74 |
| 25000.00 | 308.15 | 1072.65 |
| 25000.00 | 313.15 | 1066.6 |
| 25000.00 | 318.15 | 1060.6 |
| 25000.00 | 323.15 | 1054.58 |
| 25000.00 | 328.15 | 1048.53 |
| 30000.00 | 283.15 | 1106.39 |
| 30000.00 | 288.15 | 1100.48 |
| 30000.00 | 293.15 | 1094.5 |
| 30000.00 | 298.15 | 1088.62 |
| 30000.00 | 303.15 | 1082.75 |
| 30000.00 | 308.15 | 1076.8 |
| 30000.00 | 313.15 | 1070.82 |
| 30000.00 | 318.15 | 1064.95 |
| 30000.00 | 323.15 | 1059.07 |
| 30000.00 | 328.15 | 1053.14 |
| 35000.00 | 283.15 | 1109.85 |
| 35000.00 | 288.15 | 1104.03 |
| 35000.00 | 293.15 | 1098.19 |
| 35000.00 | 298.15 | 1092.39 |
| 35000.00 | 303.15 | 1086.6 |
| 35000.00 | 308.15 | 1080.78 |
| 35000.00 | 313.15 | 1074.93 |
| 35000.00 | 318.15 | 1069.15 |
| 35000.00 | 323.15 | 1063.39 |
| 35000.00 | 328.15 | 1057.57 |
| 40000.00 | 283.15 | 1113.17 |
| 40000.00 | 288.15 | 1107.5 |
| 40000.00 | 293.15 | 1101.74 |
| 40000.00 | 298.15 | 1096.04 |
| 40000.00 | 303.15 | 1090.35 |
| 40000.00 | 308.15 | 1084.63 |
| 40000.00 | 313.15 | 1078.87 |
| 40000.00 | 318.15 | 1073.21 |
| 40000.00 | 323.15 | 1067.56 |
| 40000.00 | 328.15 | 1061.87 |
| Reference | ||
Similar Compounds
Find more compounds similar to Carbonic acid, dimethyl ester.
Mixtures
- p-Xylene + Carbonic acid, dimethyl ester
- Carbonic acid, dimethyl ester + Decane
- p-Xylene + Carbonic acid, dimethyl ester + Decane
- Carbonic acid, dimethyl ester + Methyl Alcohol
- Carbonic acid, dimethyl ester + Water
- Carbonic acid, dimethyl ester + Methyl Alcohol + Water
- Carbonic acid, dimethyl ester + Ethanol
- Carbonic acid, dimethyl ester + Pentane, 2,2,4-trimethyl-
- Carbonic acid, dimethyl ester + Ethanol + Pentane, 2,2,4-trimethyl-
- Benzene + Carbonic acid, dimethyl ester
- Toluene + Carbonic acid, dimethyl ester
- Benzene + Carbonic acid, dimethyl ester + Ethanol
- Toluene + Carbonic acid, dimethyl ester + Ethanol
- Carbonic acid, dimethyl ester + Carbonic acid, methyl phenyl ester
- Carbonic acid, dimethyl ester + Diphenyl carbonate
- Carbonic acid, dimethyl ester + Anisole + Water
- Carbonic acid, dimethyl ester + Anisole
- Carbonic acid, dimethyl ester + Phenol
- Carbonic acid, dimethyl ester + Methyl formate
- Carbonic acid, dimethyl ester + Methylal
Find more mixtures with Carbonic acid, dimethyl ester.
Sources
- Crippen Method
- Crippen Method
- Isobaric molar heat capacities of the ternary system dimethyl carbonate + p-xylene + n-decane
- Measurements of isothermal vapor-liquid equilibrium of binary methanol/dimethyl carbonate system under pressure
- Liquid liquid equlibria of the system dimethyl carbonate + methanol +water at different temperatures
- Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
- Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes and refractive indices at 298.15K for the mixtures of di-methyl carbonate, ethanol and 2,2,4-trimethylpentane
- Vapor pressures and flash points for binary mixtures of tricyclo [5.2.1.0^(2.6)] decane and dimethyl carbonate
- High-pressure phase behavior of binary and ternary mixtures containing ionic liquid [C6-mim][Tf2N], dimethyl carbonate and carbon dioxide
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Liquid-liquid equilibria of ternary mixtures of dimethyl carbonate, diphenyl carbonate, phenol and water at 358.15 K
- Isothermal vapor-liquid equilibrium at T = 333.15 K and excess volumes and molar refractivity deviation at T = 298.15 K for the ternary mixtures {di-methyl carbonate (DMC) + ethanol + benzene} and {DMC+ ethanol + toluene}
- Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
- Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation
- Measurement of VLE data of carbon dioxide + dimethyl carbonate system for the direct synthesis of dimethyl carbonate using supercritical CO2 and methanol
- Isobaric vapor-liquid equilibrium for methanol + dimethylcarbonate + phosphoric-based ionic liquids
- Isobaric vapor-liquid equilibrium at 101.3 kPa and excess properties at 298.15 K for binary mixtures of methyl phenyl carbonate with methanol or dimethyl carbonate
- Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
- Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
- A study on the liquid-liquid equilibrium of 1-alkyl-3-methylimidazolium dialkylphosphate with methanol and dimethyl carbonate
- The solid-liquid equilitbrium, excess molar volume and refractive deviation properties of binary systems containing dimethyl carbonate, anisole and phenol
- Isobaric vapor-liquid equilibria for binary mixtures from methyl methanoate, dimethoxymethane and dimethyl carbonate at 101.33 kPa
- Ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate: An efficient entrainer to separate methanol + dimethyl carbonate azeotropic mixture
- Separation of methanol + dimethyl carbonate azeotropic mixture using ionic liquids as entrainers
- Solubilities of six lithium salts in five non-aqueous solvents and in a few of their binary mixtures
- Effect of bis(trifluoromethylsulfonyl)imide-based ionic liquids on the isobaric vapor - liquid equilibrium behavior of ethanol + dimethyl carbonate at 101.3 kPa
- Solid-liquid equilibria and thermo-physical properties of liquid electrolyte systems for lithium ion batteries
- Measurement and correlation of the isobaric vapor-liquid equilibria of methanol + methyl carbonate + Bis(trifluoromethylsulfonyl)imide-based ionic liquidsat 101.3 kPa
- Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
- Liquid-liquid measurement and correlation for separation of azeotrope (dimethyl carbonate and ethanol) with different imidazolium-based ionic liquids
- Isothermal vapor-liquid equilibria at 383.15-413.15 K for the binary system methanol + dimethyl carbonate and the pressure dependency of the azeotropic point
- Permittivity and density of binary systems of {dimethyl or diethyl carbonate} + n-dodecane from T=(288.15 to 328.15) K
- VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
- Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
- Excess molar enthalpies of dimethyl carbonate and (butanol isomers and 1-pentanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
- Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
- High-pressure phase equilibrium for the binary systems of {carbon dioxide (1) + dimethyl carbonate (2)} and {carbon dioxide (1) + diethyl carbonate (2)} at temperatures of 273 K, 283 K, and 293 K
- Vapour pressure and enthalpy of vaporization of aliphatic dialkyl carbonates
- Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
- Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
- Ebulliometric determination and prediction of (vapor + liquid) equilibria for binary and ternary mixtures containing alcohols (C1 C4) and dimethyl carbonate
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Low pressure carbon dioxide solubility in pure electrolyte solvents for lithium-ion batteries as a function of temperature. Measurement and prediction
- Measurement of (vapor + liquid) equilibrium for the systems {methanol + dimethyl carbonate} and {methanol + dimethyl carbonate + tetramethylammonium bicarbonate} at p = (34.43, 67.74) kPa
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Volumetric properties of dialkyl carbonate + n-alkane mixtures at high pressures: Experimental measurement and Nitta-Chao model prediction
- Low pressure carbon dioxide solubility in lithium-ion batteries based electrolytes as a function of temperature. Measurement and prediction
- Ternary (liquid + liquid) equilibria for (water + 1-propanol + dimethyl carbonate, or diethyl carbonate) systems at several temperatures
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Experimental and Nitta-Chao model prediction of high pressure density of p-xylene with dialkyl carbonates or n-alkanes
- Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
- Investigation of solute-solvent interactions in {1-butyl-3-methyl imidazoliumBis(trifluoromethylsulfonyl)imide + dimethylcarbonate} mixture using physicochemical properties
- Ternary liquid-liquid equilibria for systems containing (dimethyl carbonate or methyl acetate + methanol + 1-methylmidazole hydrogen sulfate) at 298.15 K and 318.15 K
- Volumetric properties of binary mixtures of ionic liquid with tributyl phosphate and dimethyl carbonate
- Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
- Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
- Thermodynamic and spectroscopic study of binary mixtures containing {dimethyl carbonate (DMC) + alcohols} at T = (288.15-308.15) K and p = (0.1-40) MPa: Experimental study and modelling
- Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
- Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
- Determination of Ternary Liquid Liquid Equilibria for Dimethyl Carbonate + 2-Methyl-1-propanol or 2-Methyl-2-propanol + Water Systems at T = 303.15 and 313.15 K
- Separation Effects of Renewable Solvent Ethyl Lactate on the Vapor Liquid Equilibria of the Methanol + Dimethyl Carbonate Azeotropic System
- Vapor Pressures and Thermophysical Properties of Dimethyl Carbonate, Diethyl Carbonate, and Dipropyl Carbonate
- Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
- Measurement and Correlation of the Electrical Conductivity of the Ionic Liquid [BMIM][TFSI] in Binary Organic Solvents
- Vapor-Liquid Equilibrium Data for Binary Mixtures of Dimethyl Carbonate with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, Isopropyl Acetate, n-Butyl Acetate, and Isoamyl Acetate at 93.13 kPa
- Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
- Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
- Ternary Liquid-Liquid Equilibrium of Toluene + Dimethyl Carbonate + ILs at 298.15 K and Atmospheric Pressure
- Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
- Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
- Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
- 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
- Solubilities of Nonpolar Gases in Triethylene Glycol Dimethyl Ether, Tetraethylene Glycol Dimethyl Ether, Dimethyl Carbonate, and Diethyl Carbonate at 298.15 K and 101.33 kPa Partial Pressure of Gas
- Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
- Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
- Vapor-Liquid Equilibria of Binary Carbon Dioxide + Alkyl Carbonate Mixture Systems
- Densities, Viscosities, and Refractive Indices of New Mixtures of Poly(ethylene glycols) + Dialkyl Carbonates at 313.15 K
- prTx Data for the Dimethyl Carbonate + Decane system
- Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
- Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
- Excess Molar Volumes and Viscosities of Binary Mixtures of Dimethyl Carbonate with Chlorobenzene, Hexane, and Heptane from (293.15 to 353.15) K and at Atmospheric Pressure
- Isobaric Vapor-Liquid Equilibria of Binary Mixtures Containing the Carbonate Group -OCOO-
- Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
- Excess Molar Enthalpies of Dimethyl Carbonate and (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
- Excess Molar Enthalpies of the Binary Carbon Dioxide + Dimethyl Carbonate System at Temperatures of (298.15 to 308.15) K and Pressures of (5.0 to 7.5) MPa
- Viscosities, Ultrasonic Velocities at (288.15 and 298.15) K, and Refractive Indices at (298.15) K of Binary Mixtures of 2,4,6-Trimethyl-1,3,5-trioxane with Dimethyl Carbonate, Diethyl Carbonate, and Propylene Carbonate
- Excess Molar Enthalpies, Molar Heat Capacities, Densities, Viscosities, and Refractive Indices of Dimethyl Sulfoxide + Esters of Carbonic Acid at 308.15 K and Atmospheric Pressure
- Ebulliometric Determination of Vapor-Liquid Equilibria for Methanol + Ethanol + Dimethyl Carbonate
- Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
- Measurement and Correlation of Vapor-Liquid Equilibria at T ) 333.15 K and Excess Molar Volumes at T ) 298.15 K for Ethanol + Dimethyl Carbonate (DMC), DMC + 1-Propanol, and DMC + 1-Butanol
- Excess Molar Volumes at 298.15 K and Isothermal Vapor-Liquid Equilibria at 333.15 K for the Binary Mixtures of Dimethyl Carbonate with Benzene, Toluene, n-Heptane, and Isooctane
- CO2 Capture with Physical Solvent Dimethyl Carbonate at High Pressures
- Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
- Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate + Methanol, + Ethanol, + Dimethyl Carbonate, or + Diethyl Carbonate at 101.3 kPa
- Density, Excess Molar Volume and Conductivity of Binary Mixtures of the Ionic Liquid 1,2-Dimethyl-3-hexylimidazolium Bis(trifluoromethylsulfonyl)imide and Dimethyl Carbonate
- Experimental Measurements and Correlations of Liquid-Liquid Equilibria for the Ternary and Quaternary Mixtures Formed by Dialkyl Carbonates at T = 298.15 K
- Solid-Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate
- Measurement and Calculation of Liquid Liquid Equilibria of Ternary and Quaternary Systems Containing Water, Propan-1-ol, and 2,2,4-Trimethylpentane (TMP) with 2,2'-Oxybis(propane) (DIPE) or Dimethyl Carbonate (DMC)
- Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + 1-Octyl-3-methylimidazolium Tetrafluoroborate
- Organic Salt Effect of Tetramethylammonium Bicarbonate on Vapor-Liquid Equilibrium of the Dimehyl Carbonate + Methanol System
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Liquid-Liquid Equilibria for the System Dimethyl Carbonate + Methanol + Glycerol in the Temperature Range of (303.15 to 333.15) K
- Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
- Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + 1-Butyl-3-methylimidazolium Dibutylphosphate
- Liquid Liquid Equilibria for Ternary Mixtures of Methylphenyl Carbonate, Dimethyl Carbonate, Diphenyl Carbonate, Anisole, Methanol, Phenol, and Water at Several Temperatures
- Liquid Phase Equilibria of the Water + Acetic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
- Liquid Phase Equilibria of Water + Formic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
- Isobaric Vapor Liquid Equilibrium for Methanol + Dimethyl Carbonate + Trifluoromethanesulfonate-based Ionic Liquids at 101.3 kPa
- Measurements and Correlation of Liquid Liquid Equilibria of (Water + Ethanol + Dimethyl Carbonate + 2,2,4-Trimethylpentane or n-Heptane) and (Water + Dimethyl Carbonate + n-Heptane + Toluene)
- Vapor-Liquid Equilibrium Data of the Binary Systems in Oxidative Carbonylation of Dimethyl Ether Synthesizing Dimethyl Carbonate
- Analysis of Surface Tension, Density, and Speed of Sound for the Ternary Mixture Dimethyl Carbonate + p-Xylene + n-Octane
- Solubility of HFC134a (1,1,1,2-Tetrafluoroethane) in Two Dialkyl Carbonates
- Mutual Diffusion Coefficients of Diethyl Carbonate and Diethyl Adipate in Heptane at T = (278.15 to 338.15) K under Atmospheric Pressure
- Densities, Viscosities, Refractive Indices, and Heat Capacities of Poly(ethylene glycol-ran-propylene glycol) + Esters of Carbonic Acid at (293.15 and 313.15) K and at Atmospheric Pressure
- Phase Behavior, Densities, and Isothermal Compressibility of (Carbon Dioxide + Dimethyl Carbonate)
- Measurements and Correlation of Liquid-Liquid Equilibria Containing Dimethyl Carbonate and Diethyl Carbonate at T = 298.15 K
- Isothermal Vapor-Liquid Equilibrium Data at T = 333.15 K and Excess Molar Volumes and Refractive Indices at T = 298.15 K for the Dimethyl Carbonate + Methanol and Isopropanol + Water with Ionic Liquids
- Joback Method
- McGowan Method
- NIST Webbook
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