- 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
- Carbonic acid, diethyl ester
- DEC
- Diaethylcarbonat
- Diatol
- Diethyl ester of carbonic acid
- Diethylester kyseliny uhlicite
- Diethylkarbonat
- Ethoxyformic anhydride
- Ethyl carbonate
- Ethyl carbonate ((EtO)2CO)
- Eufin
- NCI-C60899
- NSC 8849
- UN 2366
- ω : Acentric Factor.
- 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).
- εr : Dielectric Constant (Relative permittivity).
- 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).
- 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).
- 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.
- Ip : 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).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 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 |
|---|---|---|---|
| ω | [0.3544; 0.4561] |
|
|
| ω | 0.4561 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3544 | ChemSep v8.3 pure component data Compiled value | |
| 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° | -464.65 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-642.40; -637.90] | kJ/mol |
|
| ΔfH°gas | -639.10 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| 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° | 14.26 | 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 |
| IE | 10.14 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.97 | Relay (1.0) 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 | [3367.40; 3420.00] | kPa |
|
| Pc | 3367.40 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3420.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| 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 | |
| Ip | [1083.00; 1116.00] |
|
|
| Ip | Outlier 1083.00 | NIST | |
| Ip | Outlier 1083.00 | NIST | |
| Ip | 1100.00 | NIST | |
| Ip | 1101.00 | NIST | |
| Ip | 1116.00 | NIST | |
| Ip | 1103.00 | NIST | |
| Ip | 1104.00 | NIST | |
| Ip | 1099.00 | NIST | |
| Ip | 1102.00 | NIST | |
| Ip | 1105.00 | NIST | |
| Ip | 1105.00 | NIST | |
| Ip | 1100.00 | NIST | |
| Ip | 1099.00 | NIST | |
| Tboil | [399.00; 400.10] | K |
|
| Tboil | 399.32 | K | VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa |
| Tboil | 399.32 | K | Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa |
| Tboil | 399.60 | K | Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems |
| Tboil | 399.95 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 399.65 | K | KDB |
| Tboil | 399.20 | K | NIST |
| Tboil | 399.00 | K | NIST |
| Tboil | 399.70 ± 0.50 | K | NIST |
| Tboil | 400.10 ± 0.40 | K | NIST |
| Tboil | 400.10 ± 0.40 | K | NIST |
| Tboil | 399.70 ± 0.50 | K | NIST |
| Tboil | 399.65 ± 0.50 | K | NIST |
| Tboil | 399.10 ± 0.50 | K | NIST |
| Tc | [576.33; 578.20] | K |
|
| Tc | 578.10 | K | Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC) |
| Tc | 578.20 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tc | 576.33 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 577.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [195.86; 230.15] | K |
|
| Tfus | 195.86 | K | Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment |
| Tfus | 196.40 | K | Vapor Pressures and Thermophysical Properties of Dimethyl Carbonate, Diethyl Carbonate, and Dipropyl Carbonate |
| Tfus | 230.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 230.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 230.15 | K | KDB |
| UQi | 4.17 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.73 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.357; 0.360] | m3/kmol |
|
| Vc | 0.360 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.357 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2546760 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.25 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
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 |
|---|---|---|---|---|
| Cp,gas | [70.13; 354.87] | J/mol×K | [126.94; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 6.19220e+01 | |||
| Coefficient B | -4.95715e+02 | |||
| Coefficient C | 6.01047e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 126.94 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 70.13 | J/mol×K | 126.94 | Calculated Property |
| Cp,gas | 131.11 | J/mol×K | 279.50 | Calculated Property |
| Cp,gas | 191.35 | J/mol×K | 432.06 | Calculated Property |
| Cp,gas | 236.53 | J/mol×K | 584.62 | Calculated Property |
| Cp,gas | 270.02 | J/mol×K | 737.19 | Calculated Property |
| Cp,gas | 295.46 | J/mol×K | 889.75 | Calculated Property |
| Cp,gas | 315.30 | J/mol×K | 1042.31 | Calculated Property |
| Cp,gas | 331.16 | J/mol×K | 1194.87 | Calculated Property |
| Cp,gas | 344.11 | J/mol×K | 1347.44 | Calculated Property |
| Cp,gas | 354.87 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0013008; 0.0000680] | Pa×s | [263.15; 577.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -5.22135e+01 | |||
| Coefficient B | 2.61811e+03 | |||
| Coefficient C | 6.51693e+00 | |||
| Coefficient D | -1.00719e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 263.15 | |||
| Temperature range, max. | 577.00 | |||
| η | 0.0013008 | Pa×s | 263.15 | Calculated Property |
| η | 0.0007503 | Pa×s | 298.02 | Calculated Property |
| η | 0.0004926 | Pa×s | 332.89 | Calculated Property |
| η | 0.0003497 | Pa×s | 367.77 | Calculated Property |
| η | 0.0002599 | Pa×s | 402.64 | Calculated Property |
| η | 0.0001980 | Pa×s | 437.51 | Calculated Property |
| η | 0.0001524 | Pa×s | 472.38 | Calculated Property |
| η | 0.0001174 | Pa×s | 507.26 | Calculated Property |
| η | 0.0000899 | Pa×s | 542.13 | Calculated Property |
| η | 0.0000680 | Pa×s | 577.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [46.15; 0.00] | kJ/mol | [279.96; 577.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 5.93957e+01 | |||
| Coefficient B | 3.80000e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 5.77000e+02 | |||
| Temperature range, min. | 279.96 | |||
| Temperature range, max. | 577.00 | |||
| ΔvapH | 46.15 | kJ/mol | 279.96 | Calculated Property |
| ΔvapH | 44.13 | kJ/mol | 312.97 | Calculated Property |
| ΔvapH | 41.95 | kJ/mol | 345.97 | Calculated Property |
| ΔvapH | 39.56 | kJ/mol | 378.98 | Calculated Property |
| ΔvapH | 36.91 | kJ/mol | 411.98 | Calculated Property |
| ΔvapH | 33.91 | kJ/mol | 444.98 | Calculated Property |
| ΔvapH | 30.40 | kJ/mol | 477.99 | Calculated Property |
| ΔvapH | 26.06 | kJ/mol | 510.99 | Calculated Property |
| ΔvapH | 20.02 | kJ/mol | 544.00 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 577.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.25; 2507.12] | kPa | [273.00; 577.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.35461e+01 | |||
| Coefficient B | -2.81783e+03 | |||
| Coefficient C | -8.43040e+01 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 577.00 | |||
| Pvap | 0.25 | kPa | 273.00 | Calculated Property |
| Pvap | 2.41 | kPa | 306.78 | Calculated Property |
| Pvap | 12.80 | kPa | 340.56 | Calculated Property |
| Pvap | 46.08 | kPa | 374.33 | Calculated Property |
| Pvap | 126.96 | kPa | 408.11 | Calculated Property |
| Pvap | 288.85 | kPa | 441.89 | Calculated Property |
| Pvap | 570.23 | kPa | 475.67 | Calculated Property |
| Pvap | 1010.40 | kPa | 509.44 | Calculated Property |
| Pvap | 1645.73 | kPa | 543.22 | Calculated Property |
| Pvap | 2507.12 | kPa | 577.00 | Calculated Property |
| Pvap | [3.67e-03; 3396.12] | kPa | [230.15; 576.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.76598e+02 | |||
| Coefficient B | -1.16692e+04 | |||
| Coefficient C | -2.43764e+01 | |||
| Coefficient D | 2.02849e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| 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 |
| Pvap | [0.13; 101.60] | kPa | [263.10; 399.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.56027e+01 | |||
| Coefficient B | -3.96483e+03 | |||
| Coefficient C | -3.79590e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 263.10 | |||
| Temperature range, max. | 399.00 | |||
| Pvap | 0.13 | kPa | 263.10 | Calculated Property |
| Pvap | 0.41 | kPa | 278.20 | Calculated Property |
| Pvap | 1.08 | kPa | 293.30 | Calculated Property |
| Pvap | 2.57 | kPa | 308.40 | Calculated Property |
| Pvap | 5.57 | kPa | 323.50 | Calculated Property |
| Pvap | 11.19 | kPa | 338.60 | Calculated Property |
| Pvap | 21.02 | kPa | 353.70 | Calculated Property |
| Pvap | 37.28 | kPa | 368.80 | Calculated Property |
| Pvap | 62.91 | kPa | 383.90 | Calculated Property |
| Pvap | 101.60 | kPa | 399.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1008.79; 315.65] | kg/m3 | [263.15; 577.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 7.89116e+01 | |||
| Coefficient B | 2.50000e-01 | |||
| Coefficient C | 5.77000e+02 | |||
| Coefficient D | 2.90000e-01 | |||
| Temperature range, min. | 263.15 | |||
| Temperature range, max. | 577.00 | |||
| ρl | 1008.79 | kg/m3 | 263.15 | Calculated Property |
| ρl | 970.19 | kg/m3 | 298.02 | Calculated Property |
| ρl | 929.68 | kg/m3 | 332.89 | Calculated Property |
| ρl | 886.80 | kg/m3 | 367.77 | Calculated Property |
| ρl | 840.85 | kg/m3 | 402.64 | Calculated Property |
| ρl | 790.78 | kg/m3 | 437.51 | Calculated Property |
| ρl | 734.73 | kg/m3 | 472.38 | Calculated Property |
| ρl | 669.00 | kg/m3 | 507.26 | Calculated Property |
| ρl | 583.47 | kg/m3 | 542.13 | Calculated Property |
| ρl | 315.65 | kg/m3 | 577.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.01] | N/m | [230.15; 399.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 5.86665e-02 | |||
| Coefficient B | -1.10000e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 230.15 | |||
| Temperature range, max. | 399.15 | |||
| γ | 0.03 | N/m | 230.15 | Calculated Property |
| γ | 0.03 | N/m | 248.93 | Calculated Property |
| γ | 0.03 | N/m | 267.71 | Calculated Property |
| γ | 0.03 | N/m | 286.48 | Calculated Property |
| γ | 0.03 | N/m | 305.26 | Calculated Property |
| γ | 0.02 | N/m | 324.04 | Calculated Property |
| γ | 0.02 | N/m | 342.82 | Calculated Property |
| γ | 0.02 | N/m | 361.59 | Calculated Property |
| γ | 0.02 | N/m | 380.37 | Calculated Property |
| γ | 0.01 | N/m | 399.15 | Calculated Property |
Similar Compounds
![Ethane, 1,1'-[methylenebis(oxy)]bis-.](data:image/png;base64,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)
Find more compounds similar to Diethyl carbonate.
Mixtures
- Diethyl carbonate + Propanoic acid + Water
- Diethyl carbonate + Carbon dioxide
- Diethyl carbonate + Diphenyl carbonate
- Diethyl carbonate + Aniline
- Diethyl carbonate + Benzonitrile
- Diethyl carbonate + Benzaldehyde
- Diethyl carbonate + n-Hexane
- Diethyl carbonate + Heptane
- Diethyl carbonate + Octane
- Diethyl carbonate + Cyclohexane
- Diethyl carbonate + Ethanol
- Diethyl carbonate + Ethanol + Heptane
- Diethyl carbonate + Water
- Diethyl carbonate + Ethanol + Water
- Diethyl carbonate + 2,5,8,11-Tetraoxadodecane
- Diethyl carbonate + Acetone + Water
- Diethyl carbonate + 2-Butanone + Water
- Diethyl carbonate + 2,5,8,11,14-Pentaoxapentadecane
- Diethyl carbonate + p-Xylene
- Diethyl carbonate + Ethyl Acetate
Find more mixtures with Diethyl carbonate.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- 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
- Activity coefficients and partial molar excess enthalpies at infinite dilution for four esters in water
- 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
- On permittivity and density of the systems (tetraglyme + dimethyl or diethyl carbonate) and the formulation of De in terms of volume or mole fraction
- 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
- On permittivity and density of the systems {triglyme + (dimethyl or diethyl carbonate)} and formulation of De in terms of volume or mole fraction
- 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
- DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
- 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
- Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
- 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
- Determination of Temperature-Dependent Henry s Law Constant of Four Oxygenated Solutes in Water Using Headspace Solid-Phase Microextraction Technique
- 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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