- InChI
- InChI=1S/C5H8O4/c1-8-4(6)3-5(7)9-2/h3H2,1-2H3
- InChI Key
- BEPAFCGSDWSTEL-UHFFFAOYSA-N
- Formula
- C5H8O4
- SMILES
- COC(=O)CC(=O)OC
- Molecular Weight1
- 132.11
- CAS
- 108-59-8
- Other Names
-
- 1,3-propanedioic acid, dimethyl ester
- Dimethyl ester of malonic acid
- Dimethylmalonate
- Methyl malonate
- dimethyl 1,3-propanedioate
- dimethyl malonate
- dimethyl propanedioate
- malonic acid, dimethyl ester
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- 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).
- ΔsubH° : Enthalpy of sublimation at standard conditions (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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.8289 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | [-2311.20; -2311.20] | kJ/mol |
|
| ΔcH°liquid | -2311.20 ± 0.63 | kJ/mol | NIST |
| ΔcH°liquid | -2311.20 ± 0.63 | kJ/mol | NIST |
| ΔcH°solid | -2318.00 | kJ/mol | NIST |
| μ | 2.51 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -580.40 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-737.80; -726.50] | kJ/mol |
|
| ΔfH°gas | -726.50 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -737.80 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | -737.80 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | [-799.69; -799.69] | kJ/mol |
|
| ΔfH°liquid | -799.69 ± 0.63 | kJ/mol | NIST |
| ΔfH°liquid | -799.69 ± 0.63 | kJ/mol | NIST |
| ΔfusH° | 17.44 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 111.70 ± 2.10 | kJ/mol | NIST |
| ΔvapH° | [57.50; 61.90] | kJ/mol |
|
| ΔvapH° | 57.50 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 61.84 ± 0.79 | kJ/mol | NIST |
| ΔvapH° | 61.84 ± 0.79 | kJ/mol | NIST |
| ΔvapH° | 61.90 | kJ/mol | NIST |
| IE | 10.26 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.51 | Relay (1.0) Calculated Property | |
| logPoct/wat | -0.277 | Crippen Calculated Property | |
| McVol | 96.190 | ml/mol | McGowan Calculated Property |
| Pc | [3530.00; 4074.00] | kPa |
|
| Pc | 3530.00 | kPa | Vapor Pressures, Enthalpies of Vaporization, and Critical Parameters of a Series of Linear Aliphatic Dimethyl Esters of Dicarboxylic Acids |
| Pc | 4074.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 2.07e-06 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [882.00; 921.00] |
|
|
| Inp | 910.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 899.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 914.00 | NIST | |
| I | [1472.00; 1523.00] |
|
|
| I | 1499.00 | NIST | |
| I | 1482.00 | NIST | |
| I | 1484.00 | NIST | |
| I | 1506.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1499.00 | NIST | |
| I | 1500.00 | NIST | |
| I | 1472.00 | NIST | |
| I | Outlier 1523.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1482.00 | NIST | |
| Tboil | [452.50; 454.60] | K |
|
| Tboil | 452.50 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 454.60 | K | NIST |
| Tboil | 454.60 ± 0.80 | K | NIST |
| Tboil | 454.60 ± 0.50 | K | NIST |
| Tc | 622.40 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [211.15; 211.30] | K |
|
| Tfus | 211.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 211.30 ± 1.00 | K | NIST |
| Ttriple | 211.15 | K | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.325 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2560000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | 210.10 | J/mol×K | 298.15 | NIST |
| ΔvapH | [46.10; 61.80] | kJ/mol | [293.00; 497.00] |
|
| ΔvapH | 61.80 ± 0.80 | kJ/mol | 293.00 | NIST |
| ΔvapH | 53.70 | kJ/mol | 381.00 | NIST |
| ΔvapH | 52.90 ± 0.20 | kJ/mol | 405.50 | NIST |
| ΔvapH | 49.50 ± 0.20 | kJ/mol | 405.50 | NIST |
| ΔvapH | 46.10 ± 0.30 | kJ/mol | 405.50 | NIST |
| ΔvapH | 50.00 | kJ/mol | 497.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [141.09; 340.16] | J/mol×K | [300.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.05870e+02 | |||
| Coefficient B | 3.03520e+02 | |||
| Coefficient C | 8.13920e+02 | |||
| Coefficient D | -1.25710e+02 | |||
| Coefficient E | 1.09820e+03 | |||
| Comment | ChemSep eq 107, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 300.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 141.09 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 190.72 | J/mol×K | 433.33 | Calculated Property |
| Cp,gas | 227.41 | J/mol×K | 566.67 | Calculated Property |
| Cp,gas | 253.61 | J/mol×K | 700.00 | Calculated Property |
| Cp,gas | 274.34 | J/mol×K | 833.33 | Calculated Property |
| Cp,gas | 291.81 | J/mol×K | 966.67 | Calculated Property |
| Cp,gas | 306.82 | J/mol×K | 1100.00 | Calculated Property |
| Cp,gas | 319.72 | J/mol×K | 1233.33 | Calculated Property |
| Cp,gas | 330.75 | J/mol×K | 1366.67 | Calculated Property |
| Cp,gas | 340.16 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [185.80; 255.96] | J/mol×K | [211.15; 452.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.33040e+02 | |||
| Coefficient B | 2.30790e-01 | |||
| Coefficient C | 9.02660e-05 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidHeatCapacityCp | |||
| Temperature range, min. | 211.15 | |||
| Temperature range, max. | 452.50 | |||
| Cp,liquid | 185.80 | J/mol×K | 211.15 | Calculated Property |
| Cp,liquid | 193.07 | J/mol×K | 237.97 | Calculated Property |
| Cp,liquid | 200.48 | J/mol×K | 264.78 | Calculated Property |
| Cp,liquid | 208.01 | J/mol×K | 291.60 | Calculated Property |
| Cp,liquid | 215.68 | J/mol×K | 318.42 | Calculated Property |
| Cp,liquid | 223.47 | J/mol×K | 345.23 | Calculated Property |
| Cp,liquid | 231.40 | J/mol×K | 372.05 | Calculated Property |
| Cp,liquid | 239.46 | J/mol×K | 398.87 | Calculated Property |
| Cp,liquid | 247.64 | J/mol×K | 425.68 | Calculated Property |
| Cp,liquid | 255.96 | J/mol×K | 452.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0250641; 0.0002568] | Pa×s | [211.15; 452.50] |
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 | -1.22750e+01 | |||
| Coefficient B | 1.81350e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 211.15 | |||
| Temperature range, max. | 452.50 | |||
| η | 0.0250641 | Pa×s | 211.15 | Calculated Property |
| η | 0.0095217 | Pa×s | 237.97 | Calculated Property |
| η | 0.0044006 | Pa×s | 264.78 | Calculated Property |
| η | 0.0023441 | Pa×s | 291.60 | Calculated Property |
| η | 0.0013884 | Pa×s | 318.42 | Calculated Property |
| η | 0.0008920 | Pa×s | 345.23 | Calculated Property |
| η | 0.0006109 | Pa×s | 372.05 | Calculated Property |
| η | 0.0004402 | Pa×s | 398.87 | Calculated Property |
| η | 0.0003305 | Pa×s | 425.68 | Calculated Property |
| η | 0.0002568 | Pa×s | 452.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [64.44; 0.00] | kJ/mol | [211.15; 622.40] |
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 | 8.21050e+01 | |||
| Coefficient B | 7.06420e-01 | |||
| Coefficient C | -3.18110e-01 | |||
| Coefficient D | -1.21000e-01 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.22400e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 211.15 | |||
| Temperature range, max. | 622.40 | |||
| ΔvapH | 64.44 | kJ/mol | 211.15 | Calculated Property |
| ΔvapH | 61.12 | kJ/mol | 256.84 | Calculated Property |
| ΔvapH | 57.96 | kJ/mol | 302.54 | Calculated Property |
| ΔvapH | 54.92 | kJ/mol | 348.23 | Calculated Property |
| ΔvapH | 51.96 | kJ/mol | 393.93 | Calculated Property |
| ΔvapH | 48.99 | kJ/mol | 439.62 | Calculated Property |
| ΔvapH | 45.87 | kJ/mol | 485.32 | Calculated Property |
| ΔvapH | 42.20 | kJ/mol | 531.01 | Calculated Property |
| ΔvapH | 36.75 | kJ/mol | 576.71 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 622.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [345.14; 479.68] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.69518e+01 | |||
| Coefficient B | -5.19477e+03 | |||
| Coefficient C | -3.34050e+01 | |||
| Temperature range, min. | 345.14 | |||
| Temperature range, max. | 479.68 | |||
| Pvap | 1.33 | kPa | 345.14 | Calculated Property |
| Pvap | 2.86 | kPa | 360.09 | Calculated Property |
| Pvap | 5.73 | kPa | 375.04 | Calculated Property |
| Pvap | 10.84 | kPa | 389.99 | Calculated Property |
| Pvap | 19.49 | kPa | 404.94 | Calculated Property |
| Pvap | 33.46 | kPa | 419.88 | Calculated Property |
| Pvap | 55.20 | kPa | 434.83 | Calculated Property |
| Pvap | 87.85 | kPa | 449.78 | Calculated Property |
| Pvap | 135.37 | kPa | 464.73 | Calculated Property |
| Pvap | 202.65 | kPa | 479.68 | Calculated Property |
| Pvap | [2.07e-06; 4074.34] | kPa | [211.15; 622.40] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.84472e+01 | |||
| Coefficient B | -9.56720e+03 | |||
| Coefficient C | -8.63610e+00 | |||
| Coefficient D | 1.37230e-17 | |||
| Coefficient E | 6.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 211.15 | |||
| Temperature range, max. | 622.40 | |||
| Pvap | 2.07e-06 | kPa | 211.15 | Calculated Property |
| Pvap | 1.21e-03 | kPa | 256.84 | Calculated Property |
| Pvap | 0.08 | kPa | 302.54 | Calculated Property |
| Pvap | 1.57 | kPa | 348.23 | Calculated Property |
| Pvap | 13.48 | kPa | 393.93 | Calculated Property |
| Pvap | 68.40 | kPa | 439.62 | Calculated Property |
| Pvap | 244.86 | kPa | 485.32 | Calculated Property |
| Pvap | 698.06 | kPa | 531.01 | Calculated Property |
| Pvap | 1737.41 | kPa | 576.71 | Calculated Property |
| Pvap | 4074.34 | kPa | 622.40 | Calculated Property |
| Pvap | [0.13; 101.07] | kPa | [308.00; 453.90] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.66415e+01 | |||
| Coefficient B | -4.93597e+03 | |||
| Coefficient C | -4.34480e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 308.00 | |||
| Temperature range, max. | 453.90 | |||
| Pvap | 0.13 | kPa | 308.00 | Calculated Property |
| Pvap | 0.39 | kPa | 324.21 | Calculated Property |
| Pvap | 1.02 | kPa | 340.42 | Calculated Property |
| Pvap | 2.41 | kPa | 356.63 | Calculated Property |
| Pvap | 5.24 | kPa | 372.84 | Calculated Property |
| Pvap | 10.59 | kPa | 389.06 | Calculated Property |
| Pvap | 20.07 | kPa | 405.27 | Calculated Property |
| Pvap | 36.03 | kPa | 421.48 | Calculated Property |
| Pvap | 61.64 | kPa | 437.69 | Calculated Property |
| Pvap | 101.07 | kPa | 453.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1234.38; 406.54] | kg/m3 | [211.15; 622.40] |
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 | 1.16450e+02 | |||
| Coefficient B | 2.86440e-01 | |||
| Coefficient C | 6.22400e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 211.15 | |||
| Temperature range, max. | 622.40 | |||
| ρl | 1234.38 | kg/m3 | 211.15 | Calculated Property |
| ρl | 1189.84 | kg/m3 | 256.84 | Calculated Property |
| ρl | 1142.96 | kg/m3 | 302.54 | Calculated Property |
| ρl | 1093.17 | kg/m3 | 348.23 | Calculated Property |
| ρl | 1039.64 | kg/m3 | 393.93 | Calculated Property |
| ρl | 981.06 | kg/m3 | 439.62 | Calculated Property |
| ρl | 915.18 | kg/m3 | 485.32 | Calculated Property |
| ρl | 837.45 | kg/m3 | 531.01 | Calculated Property |
| ρl | 735.48 | kg/m3 | 576.71 | Calculated Property |
| ρl | 406.54 | kg/m3 | 622.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.05; 0.00] | N/m | [211.15; 622.40] |
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 γ in N/m, T in K | |||
| Coefficient A | 7.16060e-02 | |||
| Coefficient B | 1.04630e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.22400e+02 | |||
| Comment | ChemSep eq 106, SurfaceTension | |||
| Temperature range, min. | 211.15 | |||
| Temperature range, max. | 622.40 | |||
| γ | 0.05 | N/m | 211.15 | Calculated Property |
| γ | 0.04 | N/m | 256.84 | Calculated Property |
| γ | 0.04 | N/m | 302.54 | Calculated Property |
| γ | 0.03 | N/m | 348.23 | Calculated Property |
| γ | 0.03 | N/m | 393.93 | Calculated Property |
| γ | 0.02 | N/m | 439.62 | Calculated Property |
| γ | 0.01 | N/m | 485.32 | Calculated Property |
| γ | 0.01 | N/m | 531.01 | Calculated Property |
| γ | 0.00 | N/m | 576.71 | Calculated Property |
| γ | 0.00 | N/m | 622.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.02; 0.05] | W/m×K | [452.50; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | -5.35060e+01 | |||
| Coefficient B | 4.13370e-02 | |||
| Coefficient C | -8.66630e+05 | |||
| Coefficient D | -4.60730e+08 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 452.50 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.02 | W/m×K | 452.50 | Calculated Property |
| λ | 0.02 | W/m×K | 513.33 | Calculated Property |
| λ | 0.02 | W/m×K | 574.17 | Calculated Property |
| λ | 0.03 | W/m×K | 635.00 | Calculated Property |
| λ | 0.03 | W/m×K | 695.83 | Calculated Property |
| λ | 0.04 | W/m×K | 756.67 | Calculated Property |
| λ | 0.04 | W/m×K | 817.50 | Calculated Property |
| λ | 0.04 | W/m×K | 878.33 | Calculated Property |
| λ | 0.05 | W/m×K | 939.17 | Calculated Property |
| λ | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.16; 0.10] | W/m×K | [211.15; 452.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K | |||
| Coefficient A | 2.16390e-01 | |||
| Coefficient B | -2.49270e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidThermalConductivity | |||
| Temperature range, min. | 211.15 | |||
| Temperature range, max. | 452.50 | |||
| λ | 0.16 | W/m×K | 211.15 | Calculated Property |
| λ | 0.16 | W/m×K | 237.97 | Calculated Property |
| λ | 0.15 | W/m×K | 264.78 | Calculated Property |
| λ | 0.14 | W/m×K | 291.60 | Calculated Property |
| λ | 0.14 | W/m×K | 318.42 | Calculated Property |
| λ | 0.13 | W/m×K | 345.23 | Calculated Property |
| λ | 0.12 | W/m×K | 372.05 | Calculated Property |
| λ | 0.12 | W/m×K | 398.87 | Calculated Property |
| λ | 0.11 | W/m×K | 425.68 | Calculated Property |
| λ | 0.10 | W/m×K | 452.50 | Calculated Property |
Similar Compounds
Find more compounds similar to Propanedioic acid, dimethyl ester.
Sources
- 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 Pressures, Enthalpies of Vaporization, and Critical Parameters of a Series of Linear Aliphatic Dimethyl Esters of Dicarboxylic Acids
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.
These property values are available through the Cheméo API. A free account gives you an access key.