- InChI
- InChI=1S/C5H10O3/c1-3-7-5(6)8-4-2/h3-4H2,1-2H3
- InChI Key
- OIFBSDVPJOWBCH-UHFFFAOYSA-N
- Formula
- C5H10O3
- SMILES
- CCOC(=O)OCC
- Molecular Weight1
- 118.13
- CAS
- 105-58-8
- Other Names
-
- C2H5OC(O)OC2H5
- CARBONIC ACID,DIETHYL ESTER
- Carbonic acid, diethyl ester
- DEC
- DIATOL
- Diaethylcarbonat
- Diethyl ester of carbonic acid
- Diethylester kyseliny uhlicite
- Diethylkarbonat
- ETHYL CARBONATE
- Ethoxyformic anhydride
- Ethyl carbonate ((EtO)2CO)
- Eufin
- NCI-C60899
- NSC 8849
- UN 2366
- ΔcH°liquid : Standard liquid enthalpy of combustion (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).
- ΔfH°liquid : Liquid phase 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).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- 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
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-2715.17; -2672.50] | kJ/mol |
|
| ΔcH°liquid | -2715.17 ± 0.69 | kJ/mol | NIST |
| ΔcH°liquid | -2672.50 | kJ/mol | NIST |
| ΔfG° | -347.70 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-642.40; -637.90] | kJ/mol |
|
| ΔfH°gas | -637.90 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -642.40 ± 2.20 | kJ/mol | NIST |
| ΔfH°liquid | [-724.17; -681.50] | kJ/mol |
|
| ΔfH°liquid | -681.50 ± 0.80 | kJ/mol | NIST |
| ΔfH°liquid | -724.17 | kJ/mol | NIST |
| ΔfusH° | 12.68 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [39.10; 81.80] | kJ/mol |
|
| ΔvapH° | 43.60 | kJ/mol | NIST |
| ΔvapH° | 44.40 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 43.60 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 43.60 ± 0.15 | kJ/mol | NIST |
| ΔvapH° | 43.60 | kJ/mol | NIST |
| ΔvapH° | 39.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 81.80 | kJ/mol | NIST |
| log10WS | -0.84 | Crippen Calculated Property | |
| logPoct/wat | 1.179 | Crippen Calculated Property | |
| McVol | 94.620 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | 3589.94 | kPa | Joback Calculated Property |
| Inp | [747.00; 785.00] |
|
|
| Inp | 747.00 | NIST | |
| Inp | 747.00 | NIST | |
| Inp | 761.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 769.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 765.00 | NIST | |
| Inp | 768.00 | NIST | |
| Inp | 747.00 | NIST | |
| I | [1083.00; 1116.00] |
|
|
| I | Outlier 1083.00 | NIST | |
| I | Outlier 1083.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1101.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1103.00 | NIST | |
| I | 1104.00 | NIST | |
| I | 1099.00 | NIST | |
| I | 1102.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1099.00 | NIST | |
| Tboil | [399.32; 399.65] | K |
|
| Tboil | 399.65 | K | KDB |
| Tboil | 399.32 | K | VLE of ... |
| Tboil | 399.32 | K | Isobari... |
| Tboil | 399.60 | K | Vapor-L... |
| Tc | 578.10 | K | Measure... |
| Tfus | [195.86; 230.15] | K |
|
| Tfus | 230.15 | K | KDB |
| Tfus | 195.86 | K | Efficie... |
| Tfus | 196.40 | K | Vapor P... |
| Vc | 0.357 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [184.32; 231.33] | J/mol×K | [412.51; 591.12] |
|
| Cp,gas | 184.32 | J/mol×K | 412.51 | Joback Calculated Property |
| Cp,gas | 192.64 | J/mol×K | 442.28 | Joback Calculated Property |
| Cp,gas | 200.78 | J/mol×K | 472.05 | Joback Calculated Property |
| Cp,gas | 208.73 | J/mol×K | 501.81 | Joback Calculated Property |
| Cp,gas | 216.48 | J/mol×K | 531.58 | Joback Calculated Property |
| Cp,gas | 224.02 | J/mol×K | 561.35 | Joback Calculated Property |
| Cp,gas | 231.33 | J/mol×K | 591.12 | Joback Calculated Property |
| Cp,liquid | [182.00; 254.40] | J/mol×K | [288.15; 373.15] |
|
| Cp,liquid | 210.20 | J/mol×K | 288.15 | Densiti... |
| Cp,liquid | 219.90 | J/mol×K | 293.15 | Excess ... |
| Cp,liquid | 211.49 | J/mol×K | 293.15 | Densiti... |
| Cp,liquid | 210.90 | J/mol×K | 294.20 | NIST |
| Cp,liquid | 210.90 | J/mol×K | 294.70 | NIST |
| Cp,liquid | 182.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 221.20 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 212.46 | J/mol×K | 298.15 | Densiti... |
| Cp,liquid | 222.30 | J/mol×K | 303.15 | Excess ... |
| Cp,liquid | 213.83 | J/mol×K | 303.15 | Densiti... |
| Cp,liquid | 214.89 | J/mol×K | 308.15 | Densiti... |
| Cp,liquid | 223.40 | J/mol×K | 308.15 | Excess ... |
| Cp,liquid | 215.80 | J/mol×K | 313.15 | Densiti... |
| Cp,liquid | 225.30 | J/mol×K | 313.15 | Excess ... |
| Cp,liquid | 226.60 | J/mol×K | 318.15 | Excess ... |
| Cp,liquid | 218.55 | J/mol×K | 318.15 | Densiti... |
| Cp,liquid | 220.32 | J/mol×K | 323.15 | Densiti... |
| Cp,liquid | 228.40 | J/mol×K | 323.15 | Excess ... |
| Cp,liquid | 230.80 | J/mol×K | 328.15 | Excess ... |
| Cp,liquid | 232.00 | J/mol×K | 333.15 | Excess ... |
| Cp,liquid | 234.60 | J/mol×K | 338.15 | Excess ... |
| Cp,liquid | 237.60 | J/mol×K | 343.15 | Excess ... |
| Cp,liquid | 240.30 | J/mol×K | 348.15 | Excess ... |
| Cp,liquid | 242.50 | J/mol×K | 353.15 | Excess ... |
| Cp,liquid | 245.50 | J/mol×K | 358.15 | Excess ... |
| Cp,liquid | 248.90 | J/mol×K | 363.15 | Excess ... |
| Cp,liquid | 251.30 | J/mol×K | 368.15 | Excess ... |
| Cp,liquid | 254.40 | J/mol×K | 373.15 | Excess ... |
| η | [0.0003580; 0.0008640] | Pa×s | [288.15; 363.15] |
|
| η | 0.0008640 | Pa×s | 288.15 | Densiti... |
| η | 0.0008010 | Pa×s | 293.15 | Densiti... |
| η | 0.0008030 | Pa×s | 293.15 | Densiti... |
| η | 0.0008000 | Pa×s | 293.15 | Density... |
| η | 0.0008000 | Pa×s | 293.15 | Densiti... |
| η | 0.0008090 | Pa×s | 293.15 | Density... |
| η | 0.0007460 | Pa×s | 298.15 | Density... |
| η | 0.0007500 | Pa×s | 298.15 | Density... |
| η | 0.0007460 | Pa×s | 298.15 | Densiti... |
| η | 0.0007570 | Pa×s | 298.15 | Densiti... |
| η | 0.0006950 | Pa×s | 303.15 | Density... |
| η | 0.0007000 | Pa×s | 303.15 | Densiti... |
| η | 0.0007020 | Pa×s | 303.15 | Density... |
| η | 0.0006950 | Pa×s | 303.15 | Densiti... |
| η | 0.0006580 | Pa×s | 308.15 | Density... |
| η | 0.0006100 | Pa×s | 313.15 | Densiti... |
| η | 0.0006180 | Pa×s | 313.15 | Density... |
| η | 0.0006100 | Pa×s | 313.15 | Density... |
| η | 0.0006160 | Pa×s | 313.15 | Densiti... |
| η | 0.0005410 | Pa×s | 323.15 | Density... |
| η | 0.0005410 | Pa×s | 323.15 | Densiti... |
| η | 0.0004830 | Pa×s | 333.15 | Density... |
| η | 0.0004830 | Pa×s | 333.15 | Densiti... |
| η | 0.0004350 | Pa×s | 343.15 | Densiti... |
| η | 0.0004350 | Pa×s | 343.15 | Density... |
| η | 0.0003930 | Pa×s | 353.15 | Density... |
| η | 0.0003930 | Pa×s | 353.15 | Densiti... |
| η | 0.0003580 | Pa×s | 363.15 | Density... |
| η | 0.0003580 | Pa×s | 363.15 | Densiti... |
| ΔfusH | 9.24 | kJ/mol | 198.20 | NIST |
| ΔvapH | [39.10; 44.30] | kJ/mol | [331.00; 377.50] |
|
| ΔvapH | 44.30 | kJ/mol | 331.00 | NIST |
| ΔvapH | 39.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 40.90 | kJ/mol | 354.00 | NIST |
| ΔvapH | 42.30 | kJ/mol | 371.00 | NIST |
| ΔvapH | 39.70 | kJ/mol | 377.50 | NIST |
| Pvap | [0.29; 361.00] | kPa | [273.10; 452.20] |
|
| Pvap | 0.29 | kPa | 273.10 | Vapour ... |
| Pvap | 0.29 | kPa | 273.30 | Vapour ... |
| Pvap | 0.30 | kPa | 274.00 | Vapour ... |
| Pvap | 0.31 | kPa | 274.00 | Vapour ... |
| Pvap | 0.33 | kPa | 275.00 | Vapour ... |
| Pvap | 0.35 | kPa | 276.20 | Vapour ... |
| Pvap | 0.36 | kPa | 276.50 | Vapour ... |
| Pvap | 0.38 | kPa | 277.10 | Vapour ... |
| Pvap | 0.40 | kPa | 277.96 | Low pre... |
| Pvap | 0.41 | kPa | 278.10 | Vapour ... |
| Pvap | 0.41 | kPa | 278.20 | Vapour ... |
| Pvap | 0.52 | kPa | 282.06 | Low pre... |
| Pvap | 0.56 | kPa | 282.40 | Vapour ... |
| Pvap | 0.58 | kPa | 283.10 | Vapour ... |
| Pvap | 0.56 | kPa | 283.30 | Vapour ... |
| Pvap | 0.63 | kPa | 285.00 | Vapour ... |
| Pvap | 0.67 | kPa | 286.15 | Low pre... |
| Pvap | 0.78 | kPa | 286.80 | Vapour ... |
| Pvap | 0.80 | kPa | 288.15 | Low pre... |
| Pvap | 0.79 | kPa | 288.20 | Vapour ... |
| Pvap | 0.83 | kPa | 288.30 | Vapour ... |
| Pvap | 0.78 | kPa | 288.40 | Vapour ... |
| Pvap | 1.02 | kPa | 291.80 | Vapour ... |
| Pvap | 1.05 | kPa | 293.00 | Vapour ... |
| Pvap | 1.03 | kPa | 293.10 | Vapour ... |
| Pvap | 1.04 | kPa | 293.10 | Vapour ... |
| Pvap | 1.04 | kPa | 293.10 | Vapour ... |
| Pvap | 1.03 | kPa | 293.15 | Low pre... |
| Pvap | 1.08 | kPa | 293.20 | Vapour ... |
| Pvap | 1.06 | kPa | 293.30 | Vapour ... |
| Pvap | 1.45 | kPa | 296.80 | Vapour ... |
| Pvap | 1.49 | kPa | 298.00 | Vapour ... |
| Pvap | 1.52 | kPa | 298.10 | Vapour ... |
| Pvap | 1.45 | kPa | 298.10 | Vapour ... |
| Pvap | 1.41 | kPa | 298.15 | Low pre... |
| Pvap | 1.54 | kPa | 298.20 | Vapour ... |
| Pvap | 1.91 | kPa | 301.80 | Vapour ... |
| Pvap | 2.01 | kPa | 303.00 | Vapour ... |
| Pvap | 2.02 | kPa | 303.10 | Vapour ... |
| Pvap | 2.06 | kPa | 303.10 | Vapour ... |
| Pvap | 1.84 | kPa | 303.15 | Low pre... |
| Pvap | 1.99 | kPa | 303.15 | Measure... |
| Pvap | 1.95 | kPa | 303.15 | Measure... |
| Pvap | 1.99 | kPa | 303.30 | Vapour ... |
| Pvap | 2.35 | kPa | 306.64 | Low pre... |
| Pvap | 2.45 | kPa | 306.80 | Vapour ... |
| Pvap | 2.69 | kPa | 307.80 | Vapour ... |
| Pvap | 2.65 | kPa | 308.15 | Measure... |
| Pvap | 2.61 | kPa | 308.15 | Measure... |
| Pvap | 2.69 | kPa | 308.20 | Vapour ... |
| Pvap | 2.64 | kPa | 308.20 | Vapour ... |
| Pvap | 2.67 | kPa | 308.20 | Vapour ... |
| Pvap | 3.01 | kPa | 310.74 | Low pre... |
| Pvap | 3.07 | kPa | 310.90 | Vapour ... |
| Pvap | 3.45 | kPa | 313.15 | Measure... |
| Pvap | 3.43 | kPa | 313.15 | Measure... |
| Pvap | 3.65 | kPa | 313.30 | Vapour ... |
| Pvap | 3.96 | kPa | 315.00 | Vapour ... |
| Pvap | 3.95 | kPa | 315.20 | Vapour ... |
| Pvap | 4.58 | kPa | 318.15 | Low pre... |
| Pvap | 4.51 | kPa | 318.15 | Measure... |
| Pvap | 4.46 | kPa | 318.15 | Measure... |
| Pvap | 5.83 | kPa | 323.15 | Measure... |
| Pvap | 5.75 | kPa | 323.15 | Measure... |
| Pvap | 6.17 | kPa | 323.15 | Low pre... |
| Pvap | 7.16 | kPa | 328.15 | Low pre... |
| Pvap | 9.09 | kPa | 333.15 | Low pre... |
| Pvap | 11.56 | kPa | 338.15 | Low pre... |
| Pvap | 13.78 | kPa | 343.15 | Low pre... |
| Pvap | 13.80 | kPa | 343.77 | Density... |
| Pvap | 16.09 | kPa | 348.15 | Low pre... |
| Pvap | 19.30 | kPa | 351.67 | Density... |
| Pvap | 20.83 | kPa | 353.15 | Low pre... |
| Pvap | 20.74 | kPa | 353.15 | Isother... |
| Pvap | 22.56 | kPa | 354.68 | Phase E... |
| Pvap | 22.70 | kPa | 355.63 | Density... |
| Pvap | 25.03 | kPa | 357.44 | Phase E... |
| Pvap | 26.00 | kPa | 358.29 | Density... |
| Pvap | 27.54 | kPa | 359.95 | Phase E... |
| Pvap | 29.99 | kPa | 362.26 | Phase E... |
| Pvap | 30.23 | kPa | 363.15 | Isother... |
| Pvap | 31.30 | kPa | 363.84 | Density... |
| Pvap | 32.51 | kPa | 364.46 | Phase E... |
| Pvap | 35.05 | kPa | 366.57 | Phase E... |
| Pvap | 35.20 | kPa | 366.98 | Density... |
| Pvap | 37.52 | kPa | 368.45 | Phase E... |
| Pvap | 39.10 | kPa | 369.75 | Density... |
| Pvap | 40.03 | kPa | 370.28 | Phase E... |
| Pvap | 42.49 | kPa | 372.04 | Phase E... |
| Pvap | 42.80 | kPa | 372.28 | Density... |
| Pvap | 45.10 | kPa | 373.00 | Isother... |
| Pvap | 45.05 | kPa | 373.73 | Phase E... |
| Pvap | 46.50 | kPa | 374.61 | Density... |
| Pvap | 47.47 | kPa | 375.26 | Phase E... |
| Pvap | 50.04 | kPa | 376.81 | Phase E... |
| Pvap | 50.50 | kPa | 377.05 | Density... |
| Pvap | 52.46 | kPa | 378.22 | Phase E... |
| Pvap | 55.00 | kPa | 379.59 | Density... |
| Pvap | 55.03 | kPa | 379.67 | Phase E... |
| Pvap | 57.56 | kPa | 381.03 | Phase E... |
| Pvap | 58.80 | kPa | 381.49 | Density... |
| Pvap | 59.95 | kPa | 382.32 | Phase E... |
| Pvap | 63.10 | kPa | 383.37 | Density... |
| Pvap | 63.50 | kPa | 383.57 | Density... |
| Pvap | 62.52 | kPa | 383.60 | Phase E... |
| Pvap | 64.97 | kPa | 384.81 | Phase E... |
| Pvap | 67.44 | kPa | 385.98 | Phase E... |
| Pvap | 68.50 | kPa | 386.18 | Density... |
| Pvap | 70.02 | kPa | 387.13 | Phase E... |
| Pvap | 72.80 | kPa | 387.61 | Density... |
| Pvap | 72.51 | kPa | 388.28 | Phase E... |
| Pvap | 74.96 | kPa | 389.32 | Phase E... |
| Pvap | 78.50 | kPa | 390.35 | Density... |
| Pvap | 77.43 | kPa | 390.35 | Phase E... |
| Pvap | 79.97 | kPa | 391.39 | Phase E... |
| Pvap | 84.00 | kPa | 392.39 | Density... |
| Pvap | 82.52 | kPa | 392.45 | Phase E... |
| Pvap | 84.84 | kPa | 393.34 | Phase E... |
| Pvap | 88.20 | kPa | 393.93 | Density... |
| Pvap | 87.52 | kPa | 394.36 | Phase E... |
| Pvap | 89.81 | kPa | 395.23 | Phase E... |
| Pvap | 93.40 | kPa | 395.72 | Density... |
| Pvap | 92.53 | kPa | 396.21 | Phase E... |
| Pvap | 94.89 | kPa | 397.03 | Phase E... |
| Pvap | 97.54 | kPa | 397.96 | Phase E... |
| Pvap | 101.50 | kPa | 398.28 | Density... |
| Pvap | 100.03 | kPa | 398.81 | Phase E... |
| Pvap | 101.38 | kPa | 399.27 | Phase E... |
| Pvap | 101.30 | kPa | 399.60 | Vapor-L... |
| Pvap | 143.00 | kPa | 412.50 | Isother... |
| Pvap | 361.00 | kPa | 452.20 | Isother... |
| n0 | [1.38210; 1.38450] | [293.15; 298.15] |
|
|
| n0 | 1.38300 | 293.15 | Vapor l... | |
| n0 | 1.38450 | 293.15 | Densiti... | |
| n0 | 1.38450 | 293.15 | Densiti... | |
| n0 | 1.38280 | 298.15 | Propert... | |
| n0 | 1.38210 | 298.15 | Isobari... | |
| n0 | 1.38300 | 298.15 | Viscosi... | |
| ρl | [935.08; 980.49] | kg/m3 | [288.15; 328.15] |
|
| ρl | 980.29 | kg/m3 | 288.15 | Permitt... |
| ρl | 980.49 | kg/m3 | 288.15 | Excess ... |
| ρl | 974.91 | kg/m3 | 293.15 | Excess ... |
| ρl | 974.57 | kg/m3 | 293.15 | Permitt... |
| ρl | 974.90 | kg/m3 | 293.15 | Density... |
| ρl | 969.32 | kg/m3 | 298.15 | Influen... |
| ρl | 969.12 | kg/m3 | 298.15 | Densiti... |
| ρl | 969.23 | kg/m3 | 298.15 | Excess ... |
| ρl | 970.00 | kg/m3 | 298.15 | Low pre... |
| ρl | 969.10 | kg/m3 | 298.15 | Thermop... |
| ρl | 969.10 | kg/m3 | 298.15 | Dynamic... |
| ρl | 969.10 | kg/m3 | 298.15 | Viscosi... |
| ρl | 967.83 | kg/m3 | 298.15 | Isobari... |
| ρl | 969.30 | kg/m3 | 298.15 | Excess ... |
| ρl | 969.18 | kg/m3 | 298.15 | Solid-l... |
| ρl | 969.00 | kg/m3 | 298.15 | Isobari... |
| ρl | 969.30 | kg/m3 | 298.15 | Density... |
| ρl | 969.07 | kg/m3 | 298.15 | Permitt... |
| ρl | 969.08 | kg/m3 | 298.15 | Evaluat... |
| ρl | 963.70 | kg/m3 | 303.15 | Density... |
| ρl | 963.66 | kg/m3 | 303.15 | Excess ... |
| ρl | 963.60 | kg/m3 | 303.15 | Permitt... |
| ρl | 963.50 | kg/m3 | 303.15 | Thermop... |
| ρl | 958.00 | kg/m3 | 308.15 | Density... |
| ρl | 958.00 | kg/m3 | 308.15 | Excess ... |
| ρl | 957.80 | kg/m3 | 308.15 | Thermop... |
| ρl | 957.90 | kg/m3 | 308.15 | Excess ... |
| ρl | 957.98 | kg/m3 | 308.15 | Permitt... |
| ρl | 952.43 | kg/m3 | 313.15 | Densiti... |
| ρl | 952.40 | kg/m3 | 313.15 | Density... |
| ρl | 952.10 | kg/m3 | 313.15 | Thermop... |
| ρl | 952.32 | kg/m3 | 313.15 | Excess ... |
| ρl | 952.15 | kg/m3 | 313.15 | Densiti... |
| ρl | 946.70 | kg/m3 | 318.15 | Density... |
| ρl | 947.67 | kg/m3 | 318.15 | Permitt... |
| ρl | 946.40 | kg/m3 | 318.15 | Thermop... |
| ρl | 946.60 | kg/m3 | 318.15 | Excess ... |
| ρl | 940.86 | kg/m3 | 323.15 | Excess ... |
| ρl | 940.70 | kg/m3 | 323.15 | Thermop... |
| ρl | 940.90 | kg/m3 | 323.15 | Density... |
| ρl | 935.08 | kg/m3 | 328.15 | Excess ... |
| ρl | 935.12 | kg/m3 | 328.15 | Permitt... |
| ρl | 935.20 | kg/m3 | 328.15 | Density... |
| csound,fluid | 1178.00 | m/s | 298.15 | Vapor l... |
| γ | [0.02; 0.03] | N/m | [273.18; 373.17] |
|
| γ | 0.03 | N/m | 273.18 | Surface... |
| γ | 0.03 | N/m | 278.18 | Surface... |
| γ | 0.03 | N/m | 283.18 | Surface... |
| γ | 0.03 | N/m | 288.18 | Surface... |
| γ | 0.03 | N/m | 293.16 | Surface... |
| γ | 0.03 | N/m | 298.10 | Surface... |
| γ | 0.03 | N/m | 298.15 | Surface... |
| γ | 0.03 | N/m | 303.17 | Surface... |
| γ | 0.03 | N/m | 308.11 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 313.19 | Surface... |
| γ | 0.02 | N/m | 318.16 | Surface... |
| γ | 0.02 | N/m | 323.16 | Surface... |
| γ | 0.02 | N/m | 328.12 | Surface... |
| γ | 0.02 | N/m | 333.18 | Surface... |
| γ | 0.02 | N/m | 338.17 | Surface... |
| γ | 0.02 | N/m | 343.17 | Surface... |
| γ | 0.02 | N/m | 348.17 | Surface... |
| γ | 0.02 | N/m | 353.19 | Surface... |
| γ | 0.02 | N/m | 358.18 | Surface... |
| γ | 0.02 | N/m | 363.16 | Surface... |
| γ | 0.02 | N/m | 368.18 | Surface... |
| γ | 0.02 | N/m | 373.17 | Surface... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 980.3 |
| 288.15 | 5000.00 | 984.5 |
| 288.15 | 10000.00 | 988.6 |
| 288.15 | 20000.00 | 996.3 |
| 288.15 | 30000.00 | 1003.6 |
| 288.15 | 40000.00 | 1010.5 |
| 298.15 | 100.00 | 968.9 |
| 298.15 | 5000.00 | 973.8 |
| 298.15 | 10000.00 | 977.8 |
| 298.15 | 20000.00 | 986.0 |
| 298.15 | 30000.00 | 993.6 |
| 298.15 | 40000.00 | 1000.8 |
| 308.15 | 100.00 | 957.7 |
| 308.15 | 5000.00 | 962.4 |
| 308.15 | 10000.00 | 967.1 |
| 308.15 | 20000.00 | 975.7 |
| 308.15 | 30000.00 | 983.8 |
| 308.15 | 40000.00 | 991.3 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 969.3 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 969.4 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [3.67e-03; 3396.12] | kPa | [230.15; 576.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.76598e+02 | |||
| Coefficient B | -1.16692e+04 | |||
| Coefficient C | -2.43764e+01 | |||
| Coefficient D | 2.02849e-05 | |||
| Temperature range, min. | 230.15 | |||
| Temperature range, max. | 576.00 | |||
| Pvap | 3.67e-03 | kPa | 230.15 | Calculated Property |
| Pvap | 0.18 | kPa | 268.58 | Calculated Property |
| Pvap | 2.46 | kPa | 307.01 | Calculated Property |
| Pvap | 15.84 | kPa | 345.43 | Calculated Property |
| Pvap | 62.89 | kPa | 383.86 | Calculated Property |
| Pvap | 183.16 | kPa | 422.29 | Calculated Property |
| Pvap | 437.25 | kPa | 460.72 | Calculated Property |
| Pvap | 921.36 | kPa | 499.14 | Calculated Property |
| Pvap | 1803.01 | kPa | 537.57 | Calculated Property |
| Pvap | 3396.12 | kPa | 576.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Diethyl carbonate.
Mixtures
- Diethyl carbonate + Carbon dioxide
- Diethyl carbonate + Acetone
- Diethyl carbonate + 2-Butanone
- Diethyl carbonate + 2-Pentanone
- Diethyl carbonate + Ethanol
- Diethyl carbonate + Water
- Diethyl carbonate + Ethanol + Water
- Diethyl carbonate + n-Hexane
- Diethyl carbonate + Heptane
- Diethyl carbonate + Octane
- Diethyl carbonate + Cyclohexane
- Diethyl carbonate + Ethanol + Heptane
- Diethyl carbonate + Diphenyl carbonate
- Diethyl carbonate + Dodecane
- Diethyl carbonate + Cyclohexane, methyl-
- Diethyl carbonate + Acetophenone
- Diethyl carbonate + 1-Hexanol
- Diethyl carbonate + p-Xylene
- Diethyl carbonate + Decane
- Diethyl carbonate + p-Xylene + Decane
Find more mixtures with Diethyl carbonate.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Vapor liquid equilibria of carbon dioxide with isopropyl acetate, diethyl carbonate and ethyl butyrate at elevated pressures
- Excess molar enthalpies for binary carbon dioxide + diethyl carbonate system at 298.15 - 308.15K and 5.0 - 6.5MPa
- Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
- Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
- Vapor-liquid equilibrium data for the binary systems in the process of synthesizing diethyl carbonate
- Separation of propionic acid by diethyl carbonate or diethyl malonate or diethyl fumarate and the synergistic effect of phosphorus compounds and amines
- Surface tension of diethyl carbonate, 1,2-dimethoxyethane and diethyl adipate
- Liquid phase equilibria of (water + formic acid + diethyl carbonate or diethyl malonate or diethyl fumarate) ternary systems at 298.15K and atmospheric pressure
- Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
- Isothermal vapor liquid and vapor liquid liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
- Ionic interplay of lithium salts in binary mixtures of acetonitrile and diethyl carbonate probed by physicochemical approach
- Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
- Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
- 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
- Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
- Densities and derived thermodynamic properties of binary mixtures of diethylcarbonate, acetophenone, and 1-hexanol at T = (293.15 to 323.15) K for the liquid region and at ambient pressure
- 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
- Surface tension, density, and speed of sound for the ternary mixture {diethyl carbonate + p-xylene + decane}
- Thermophysical properties for (diethyl carbonate + p-xylene + octane) ternary system
- Low pressure carbon dioxide solubility in pure electrolyte solvents for lithium-ion batteries as a function of temperature. Measurement and prediction
- 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
- Experimental and Nitta-Chao model prediction of high pressure density of p-xylene with dialkyl carbonates or n-alkanes
- Effect of temperature on density, sound velocity, refractive index and their derived properties for the binary systems (heptanoic acid + propanoic or butanoic acids)
- Low pressure methane solubility in lithium-ion batteries based solvents and electrolytes as a function of temperature. Measurement and prediction
- Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
- Phase equilibria of the ternary systems of (water + diethyl carbonate) with acetone, or 2-butanone at four temperatures
- Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
- Study of molecular interactions of binary mixtures DEC with alkoxyalkanols at various temperatures
- Density and viscosity of four binary mixtures of [C2mmim][NTf2]/[C4mmim][NTf2] + dimethyl carbonate/diethyl carbonate
- Influence of alkyl group and temperature on thermophysical properties of carboxylic acid and their binary mixtures
- Isobaric Vapor Liquid Equilibria for Binary Systems of Diethyl Carbonate + Propylene Carbonate, Diethyl Carbonate + Propylene Glycol, and Ethanol + Propylene Carbonate at 101.3 kPa
- Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
- 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
- Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
- Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
- Vapor Pressures and Thermophysical Properties of Dimethyl Carbonate, Diethyl Carbonate, and Dipropyl Carbonate
- Excess Molar Volume and Viscosity Deviation of [C2mim][NTf2]/[C4mim][NTf2] + DMC/DEC
- Atmospheric Ternary Liquid-Liquid Equilibrium for the Diethyl Carbonate + 1-Propanol + Water System at Temperature of 303.15, 313.15, 323.15, and 333.15 K
- Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Methyl Acetate, n-Propyl Acetate, or Amyl Acetate at 100.17 kPa
- Isobaric Vapor-Liquid Equilibria of Binary Mixtures of Diethyl Carbonate with Isopropyl Acetate, sec-Butyl Acetate, or Isoamyl Acetate at 101.3 kPa
- Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
- Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
- 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
- Vapor-Liquid Equilibria of Binary Carbon Dioxide + Alkyl Carbonate Mixture Systems
- Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
- Densities, Viscosities, and Refractive Indices of New Mixtures of Poly(ethylene glycols) + Dialkyl Carbonates at 313.15 K
- Excess Enthalpies, Densities, Viscosities, and Refractive Indices of Binary Mixtures Involving Some Poly(glycols) + Diethyl Carbonate at 308.15 K
- Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
- Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
- Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
- 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
- Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
- 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
- Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
- Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
- Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate + Methanol, + Ethanol, + Dimethyl Carbonate, or + Diethyl Carbonate at 101.3 kPa
- Experimental Measurements and Correlations of Liquid-Liquid Equilibria for the Ternary and Quaternary Mixtures Formed by Dialkyl Carbonates at T = 298.15 K
- Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
- Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
- Liquid Liquid Equilibrium for the Water + Diethyl Carbonate + Ethanol System at Different Temperatures
- Surface Tension of Dialkyl Carbonates + (Alkanes or 1,4-Dimethylbenzene) and 1,4-Dimethylbenzene + Alkanes Binary Mixtures at T = 308.15 K
- Liquid Liquid Equilibria for Quaternary Systems of Water + Ethanol + Diethyl Carbonate + Methylbenzene or Heptane
- Densities, Viscosities, Speeds of Sound, and Refractive Indices for Binary Mixtures of Diethylcarbonate, Acetophenone, and 1-Hexanol at (293.15, 303.15, 313.15, and 323.15) K for the Liquid Region and at Ambient Pressure
- Density, Viscosity, and Vapor Pressure for Binary Mixtures of Tricyclo [5.2.1.02.6] Decane and Diethyl Carbonate
- 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
- Measurements and Correlation of Liquid-Liquid Equilibria Containing Dimethyl Carbonate and Diethyl Carbonate at T = 298.15 K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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