- InChI
- InChI=1S/C3H8O/c1-3-4-2/h3H2,1-2H3
- InChI Key
- XOBKSJJDNFUZPF-UHFFFAOYSA-N
- Formula
- C3H8O
- SMILES
- CCOC
- Molecular Weight1
- 60.10
- CAS
- 540-67-0
- Other Names
-
- C2H5OCH3
- ETHOXY METHANE
- Ether, ethyl methyl
- Ethyl methyl ether
- Methane, ethoxy-
- Methoxyethane
- Methyl ethyl ether
- UN 1039
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°gas : Standard gas 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).
- ΔfusH° : Enthalpy of fusion 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- 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).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2360; 0.2440] |
|
|
| ω | 0.2361 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2360 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2440 | KDB | |
| PAff | 808.60 | kJ/mol | NIST |
| BasG | 781.20 | kJ/mol | NIST |
| ΔcH°gas | -2107.40 ± 0.63 | kJ/mol | NIST |
| μ | [1.20; 1.23] | debye |
|
| μ | 1.23 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 1.20 | debye | KDB |
| ΔfG° | [-117.70; -117.70] | kJ/mol |
|
| ΔfG° | -117.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -117.70 | kJ/mol | KDB |
| ΔfH°gas | [-216.60; -216.40] | kJ/mol |
|
| ΔfH°gas | -216.40 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -216.60 | kJ/mol | KDB |
| ΔfH°gas | -216.40 ± 0.67 | kJ/mol | NIST |
| ΔfusH° | 4.71 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 22.70 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [9.50; 9.86] | eV |
|
| IE | 9.72 ± 0.07 | eV | NIST |
| IE | 9.72 ± 0.07 | eV | NIST |
| IE | 9.86 | eV | NIST |
| IE | 9.72 | eV | NIST |
| IE | 9.50 | eV | NIST |
| IE | 9.60 ± 0.10 | eV | NIST |
| IE | 9.72 | eV | NIST |
| IE | 9.81 | eV | NIST |
| log10WS | 0.21 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.653 | Crippen Calculated Property | |
| McVol | 59.000 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 4 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [4361.00; 4688.00] | kPa |
|
| Pc | 4380.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 4397.51 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4400.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 4400.00 | kPa | KDB |
| Pc | 4361.00 ± 50.66 | kPa | NIST |
| Pc | 4400.00 ± 40.53 | kPa | NIST |
| Pc | Outlier 4688.00 ± 303.98 | kPa | NIST |
| Ptriple | 7.85e-03 | kPa | ChemSep v8.3 pure component data Compiled value |
| ρc | [272.17; 307.03] | kg/m3 |
|
| ρc | 272.17 ± 1.80 | kg/m3 | NIST |
| ρc | 307.03 ± 19.83 | kg/m3 | NIST |
| Inp | [419.00; 421.00] |
|
|
| Inp | 421.00 | NIST | |
| Inp | 421.00 | NIST | |
| Inp | 419.00 | NIST | |
| Inp | 421.00 | NIST | |
| Tboil | [279.75; 312.10] | K |
|
| Tboil | 280.50 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 280.60 | K | KDB |
| Tboil | 283.20 | K | NIST |
| Tboil | 312.10 ± 0.40 | K | NIST |
| Tboil | 279.75 ± 0.60 | K | NIST |
| Tc | [437.80; 441.60] | K |
|
| Tc | 437.90 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 437.80 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 437.80 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 438.15 | K | Air Liquide Gas Encyclopedia |
| Tc | 437.80 | K | KDB |
| Tc | 438.03 ± 1.00 | K | NIST |
| Tc | 437.80 ± 0.30 | K | NIST |
| Tc | 437.90 ± 0.30 | K | NIST |
| Tc | Outlier 441.60 ± 4.00 | K | NIST |
| Tc | 440.90 ± 3.00 | K | NIST |
| Tfus | [134.15; 160.15] | K |
|
| Tfus | 160.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 160.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 134.15 | K | Air Liquide Gas Encyclopedia |
| Tfus | 160.00 | K | KDB |
| Ttriple | 160.00 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 2.48 | ChemSep v8.3 pure component data Compiled value | |
| URi | 2.72 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.221; 0.222] | m3/kmol |
|
| Vc | 0.222 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Vc | 0.221 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.221 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.221 | m3/kmol | KDB |
| Vc | 0.222 ± 0.003 | m3/kmol | NIST |
| Zc | [0.2670000; 0.2671360] |
|
|
| Zc | 0.2670000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value | |
| Zc | 0.2670000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2671360 | KDB | |
| Zra | 0.27 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [24.69; 37.10] | kJ/mol | [231.00; 359.50] |
|
| ΔvapH | 26.30 | kJ/mol | 231.00 | NIST |
| ΔvapH | 37.00 | kJ/mol | 257.50 | NIST |
| ΔvapH | 24.69 | kJ/mol | 280.80 | KDB |
| ΔvapH | 30.10 | kJ/mol | 357.00 | NIST |
| ΔvapH | 37.10 | kJ/mol | 359.50 | NIST |
| ρl | 700.00 | kg/m3 | 293.00 | KDB |
| γ | 0.02 | N/m | 298.20 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [65.17; 228.83] | J/mol×K | [150.00; 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 | 6.05710e+01 | |||
| Coefficient B | -5.57180e+02 | |||
| Coefficient C | 5.17124e+00 | |||
| Coefficient D | 4.80840e-04 | |||
| Coefficient E | -1.75810e-07 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 65.17 | J/mol×K | 150.00 | Calculated Property |
| Cp,gas | 91.83 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 121.75 | J/mol×K | 450.00 | Calculated Property |
| Cp,gas | 147.74 | J/mol×K | 600.00 | Calculated Property |
| Cp,gas | 169.43 | J/mol×K | 750.00 | Calculated Property |
| Cp,gas | 187.36 | J/mol×K | 900.00 | Calculated Property |
| Cp,gas | 201.98 | J/mol×K | 1050.00 | Calculated Property |
| Cp,gas | 213.62 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 222.51 | J/mol×K | 1350.00 | Calculated Property |
| Cp,gas | 228.83 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [117.49; 145.10] | J/mol×K | [160.00; 291.87] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.09050e+02 | |||
| Coefficient B | -3.16450e+01 | |||
| Coefficient C | 8.70545e-01 | |||
| Coefficient D | 8.46840e-03 | |||
| Coefficient E | 4.12020e-06 | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 291.87 | |||
| Cp,liquid | 117.49 | J/mol×K | 160.00 | Calculated Property |
| Cp,liquid | 118.97 | J/mol×K | 174.65 | Calculated Property |
| Cp,liquid | 120.69 | J/mol×K | 189.30 | Calculated Property |
| Cp,liquid | 122.70 | J/mol×K | 203.96 | Calculated Property |
| Cp,liquid | 125.07 | J/mol×K | 218.61 | Calculated Property |
| Cp,liquid | 127.86 | J/mol×K | 233.26 | Calculated Property |
| Cp,liquid | 131.15 | J/mol×K | 247.91 | Calculated Property |
| Cp,liquid | 135.04 | J/mol×K | 262.57 | Calculated Property |
| Cp,liquid | 139.64 | J/mol×K | 277.22 | Calculated Property |
| Cp,liquid | 145.10 | J/mol×K | 291.87 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0009134; 0.0001003] | Pa×s | [160.00; 373.15] |
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 | -1.11380e+01 | |||
| Coefficient B | 6.28050e+02 | |||
| Coefficient C | 4.23450e-02 | |||
| Coefficient D | -2.02810e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 373.15 | |||
| η | 0.0009134 | Pa×s | 160.00 | Calculated Property |
| η | 0.0005538 | Pa×s | 183.68 | Calculated Property |
| η | 0.0003766 | Pa×s | 207.37 | Calculated Property |
| η | 0.0002773 | Pa×s | 231.05 | Calculated Property |
| η | 0.0002162 | Pa×s | 254.73 | Calculated Property |
| η | 0.0001759 | Pa×s | 278.42 | Calculated Property |
| η | 0.0001479 | Pa×s | 302.10 | Calculated Property |
| η | 0.0001275 | Pa×s | 325.78 | Calculated Property |
| η | 0.0001122 | Pa×s | 349.47 | Calculated Property |
| η | 0.0001003 | Pa×s | 373.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [29.82; 9.82] | kJ/mol | [160.00; 423.18] |
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 | 1.36790e+02 | |||
| Coefficient B | 9.49480e+00 | |||
| Coefficient C | -2.56550e+01 | |||
| Coefficient D | 2.84240e+01 | |||
| Coefficient E | -1.16030e+01 | |||
| Critical temperature, Tc (K) | 4.37800e+02 | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 423.18 | |||
| ΔvapH | 29.82 | kJ/mol | 160.00 | Calculated Property |
| ΔvapH | 28.37 | kJ/mol | 189.24 | Calculated Property |
| ΔvapH | 27.35 | kJ/mol | 218.48 | Calculated Property |
| ΔvapH | 26.29 | kJ/mol | 247.73 | Calculated Property |
| ΔvapH | 24.86 | kJ/mol | 276.97 | Calculated Property |
| ΔvapH | 22.93 | kJ/mol | 306.21 | Calculated Property |
| ΔvapH | 20.51 | kJ/mol | 335.45 | Calculated Property |
| ΔvapH | 17.76 | kJ/mol | 364.70 | Calculated Property |
| ΔvapH | 14.66 | kJ/mol | 393.94 | Calculated Property |
| ΔvapH | 9.82 | kJ/mol | 423.18 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 3537.71] | kPa | [217.94; 437.80] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.23480e+01 | |||
| Coefficient B | -1.40486e+03 | |||
| Coefficient C | -1.01451e+02 | |||
| Temperature range, min. | 217.94 | |||
| Temperature range, max. | 437.80 | |||
| Pvap | 1.33 | kPa | 217.94 | Calculated Property |
| Pvap | 10.79 | kPa | 242.37 | Calculated Property |
| Pvap | 47.07 | kPa | 266.80 | Calculated Property |
| Pvap | 140.51 | kPa | 291.23 | Calculated Property |
| Pvap | 326.86 | kPa | 315.66 | Calculated Property |
| Pvap | 639.65 | kPa | 340.08 | Calculated Property |
| Pvap | 1105.02 | kPa | 364.51 | Calculated Property |
| Pvap | 1739.59 | kPa | 388.94 | Calculated Property |
| Pvap | 2550.68 | kPa | 413.37 | Calculated Property |
| Pvap | 3537.71 | kPa | 437.80 | Calculated Property |
| Pvap | [0.01; 4401.90] | kPa | [160.00; 437.80] |
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 | 5.69322e+01 | |||
| Coefficient B | -4.65920e+03 | |||
| Coefficient C | -6.41370e+00 | |||
| Coefficient D | 5.77270e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 437.85 K. | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 437.80 | |||
| Pvap | 0.01 | kPa | 160.00 | Calculated Property |
| Pvap | 0.39 | kPa | 190.87 | Calculated Property |
| Pvap | 4.76 | kPa | 221.73 | Calculated Property |
| Pvap | 29.26 | kPa | 252.60 | Calculated Property |
| Pvap | 114.53 | kPa | 283.47 | Calculated Property |
| Pvap | 329.79 | kPa | 314.33 | Calculated Property |
| Pvap | 765.54 | kPa | 345.20 | Calculated Property |
| Pvap | 1521.76 | kPa | 376.07 | Calculated Property |
| Pvap | 2699.87 | kPa | 406.93 | Calculated Property |
| Pvap | 4401.90 | kPa | 437.80 | Calculated Property |
| Pvap | [3.35e-04; 4647.74] | kPa | [160.00; 437.80] |
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 | 2.43488e+02 | |||
| Coefficient B | -1.12818e+04 | |||
| Coefficient C | -3.58975e+01 | |||
| Coefficient D | 4.71928e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 437.80 | |||
| Pvap | 3.35e-04 | kPa | 160.00 | Calculated Property |
| Pvap | 0.09 | kPa | 190.87 | Calculated Property |
| Pvap | 2.80 | kPa | 221.73 | Calculated Property |
| Pvap | 26.01 | kPa | 252.60 | Calculated Property |
| Pvap | 117.24 | kPa | 283.47 | Calculated Property |
| Pvap | 341.34 | kPa | 314.33 | Calculated Property |
| Pvap | 765.38 | kPa | 345.20 | Calculated Property |
| Pvap | 1479.02 | kPa | 376.07 | Calculated Property |
| Pvap | 2653.25 | kPa | 406.93 | Calculated Property |
| Pvap | 4647.74 | kPa | 437.80 | Calculated Property |
| Pvap | [0.13; 101.21] | kPa | [182.00; 280.70] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.38915e+01 | |||
| Coefficient B | -2.19348e+03 | |||
| Coefficient C | -4.41890e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 182.00 | |||
| Temperature range, max. | 280.70 | |||
| Pvap | 0.13 | kPa | 182.00 | Calculated Property |
| Pvap | 0.43 | kPa | 192.97 | Calculated Property |
| Pvap | 1.17 | kPa | 203.93 | Calculated Property |
| Pvap | 2.84 | kPa | 214.90 | Calculated Property |
| Pvap | 6.16 | kPa | 225.87 | Calculated Property |
| Pvap | 12.25 | kPa | 236.83 | Calculated Property |
| Pvap | 22.62 | kPa | 247.80 | Calculated Property |
| Pvap | 39.22 | kPa | 258.77 | Calculated Property |
| Pvap | 64.47 | kPa | 269.73 | Calculated Property |
| Pvap | 101.21 | kPa | 280.70 | Calculated Property |
| Pvap | [93.15; 4030.74] | kPa | [280.70; 433.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.25606e+01 | |||
| Coefficient B | -1.38186e+03 | |||
| Coefficient C | -1.08534e+02 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 280.70 | |||
| Temperature range, max. | 433.00 | |||
| Pvap | 93.15 | kPa | 280.70 | Calculated Property |
| Pvap | 191.06 | kPa | 297.62 | Calculated Property |
| Pvap | 348.23 | kPa | 314.54 | Calculated Property |
| Pvap | 579.42 | kPa | 331.47 | Calculated Property |
| Pvap | 897.26 | kPa | 348.39 | Calculated Property |
| Pvap | 1311.63 | kPa | 365.31 | Calculated Property |
| Pvap | 1829.42 | kPa | 382.23 | Calculated Property |
| Pvap | 2454.64 | kPa | 399.16 | Calculated Property |
| Pvap | 3188.69 | kPa | 416.08 | Calculated Property |
| Pvap | 4030.74 | kPa | 433.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [837.49; 293.88] | kg/m3 | [160.00; 437.80] |
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 | 6.72764e+01 | |||
| Coefficient B | 2.63670e-01 | |||
| Coefficient C | 4.37860e+02 | |||
| Coefficient D | 2.52310e-01 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 437.85 K. | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 437.80 | |||
| ρl | 837.49 | kg/m3 | 160.00 | Calculated Property |
| ρl | 808.85 | kg/m3 | 190.87 | Calculated Property |
| ρl | 778.53 | kg/m3 | 221.73 | Calculated Property |
| ρl | 746.10 | kg/m3 | 252.60 | Calculated Property |
| ρl | 710.97 | kg/m3 | 283.47 | Calculated Property |
| ρl | 672.20 | kg/m3 | 314.33 | Calculated Property |
| ρl | 628.15 | kg/m3 | 345.20 | Calculated Property |
| ρl | 575.50 | kg/m3 | 376.07 | Calculated Property |
| ρl | 505.17 | kg/m3 | 406.93 | Calculated Property |
| ρl | 293.88 | kg/m3 | 437.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.02] | N/m | [160.15; 280.55] |
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 | 5.45339e-02 | |||
| Coefficient B | -1.31700e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 160.15 | |||
| Temperature range, max. | 280.55 | |||
| γ | 0.03 | N/m | 160.15 | Calculated Property |
| γ | 0.03 | N/m | 173.53 | Calculated Property |
| γ | 0.03 | N/m | 186.91 | Calculated Property |
| γ | 0.03 | N/m | 200.28 | Calculated Property |
| γ | 0.03 | N/m | 213.66 | Calculated Property |
| γ | 0.02 | N/m | 227.04 | Calculated Property |
| γ | 0.02 | N/m | 240.42 | Calculated Property |
| γ | 0.02 | N/m | 253.79 | Calculated Property |
| γ | 0.02 | N/m | 267.17 | Calculated Property |
| γ | 0.02 | N/m | 280.55 | Calculated Property |
| γ | [0.03; 9.20e-04] | N/m | [160.00; 423.18] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.01650e-02 | |||
| Coefficient B | 6.68370e+01 | |||
| Coefficient C | -3.70840e+00 | |||
| Coefficient D | 3.14290e-03 | |||
| Coefficient E | -1.27410e-05 | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 423.18 | |||
| γ | 0.03 | N/m | 160.00 | Calculated Property |
| γ | 0.03 | N/m | 189.24 | Calculated Property |
| γ | 0.03 | N/m | 218.48 | Calculated Property |
| γ | 0.02 | N/m | 247.73 | Calculated Property |
| γ | 0.02 | N/m | 276.97 | Calculated Property |
| γ | 0.01 | N/m | 306.21 | Calculated Property |
| γ | 0.01 | N/m | 335.45 | Calculated Property |
| γ | 0.01 | N/m | 364.70 | Calculated Property |
| γ | 0.00 | N/m | 393.94 | Calculated Property |
| γ | 9.20e-04 | N/m | 423.18 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.09] | W/m×K | [160.00; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 2.10580e-04 | |||
| Coefficient B | 9.44720e-01 | |||
| Coefficient C | 5.15360e+02 | |||
| Coefficient D | 8.10830e+03 | |||
| Temperature range, min. | 160.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 160.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 253.33 | Calculated Property |
| λgas | 0.02 | W/m×K | 346.67 | Calculated Property |
| λgas | 0.03 | W/m×K | 440.00 | Calculated Property |
| λgas | 0.04 | W/m×K | 533.33 | Calculated Property |
| λgas | 0.05 | W/m×K | 626.67 | Calculated Property |
| λgas | 0.06 | W/m×K | 720.00 | Calculated Property |
| λgas | 0.07 | W/m×K | 813.33 | Calculated Property |
| λgas | 0.08 | W/m×K | 906.67 | Calculated Property |
| λgas | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.22; 0.10] | W/m×K | [123.15; 393.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.90030e-02 | |||
| Coefficient B | 3.41240e+01 | |||
| Coefficient C | -1.93560e+00 | |||
| Coefficient D | 1.02950e-03 | |||
| Coefficient E | -7.99390e-06 | |||
| Temperature range, min. | 123.15 | |||
| Temperature range, max. | 393.15 | |||
| λliquid | 0.22 | W/m×K | 123.15 | Calculated Property |
| λliquid | 0.20 | W/m×K | 153.15 | Calculated Property |
| λliquid | 0.19 | W/m×K | 183.15 | Calculated Property |
| λliquid | 0.18 | W/m×K | 213.15 | Calculated Property |
| λliquid | 0.16 | W/m×K | 243.15 | Calculated Property |
| λliquid | 0.15 | W/m×K | 273.15 | Calculated Property |
| λliquid | 0.13 | W/m×K | 303.15 | Calculated Property |
| λliquid | 0.12 | W/m×K | 333.15 | Calculated Property |
| λliquid | 0.11 | W/m×K | 363.15 | Calculated Property |
| λliquid | 0.10 | W/m×K | 393.15 | Calculated Property |
Similar Compounds
![Ethane, 1,1'-[methylenebis(oxy)]bis-.](data:image/png;base64,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)
Find more compounds similar to Ethane, methoxy-.
Sources
- KDB Vapor Pressure Data
- Air Liquide Gas Encyclopedia
- 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).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- 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
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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