- InChI
- InChI=1S/C3H8O2/c1-4-3-5-2/h3H2,1-2H3
- InChI Key
- NKDDWNXOKDWJAK-UHFFFAOYSA-N
- Formula
- C3H8O2
- SMILES
- COCOC
- Molecular Weight1
- 76.09
- CAS
- 109-87-5
- Other Names
-
- (CH3O)2CH2
- 2,4-dioxapentane
- Anesthenyl
- Bis(methoxy)methane
- Dimethylacetal formaldehyde
- Formal
- Formaldehyde dimethyl acetal
- Formaldehyde methyl ketal
- Methoxymethyl methyl ether
- Methylene dimethyl ether
- Methylene glycol dimethylether
- Methylenedioxydimethane
- Metylal
- UN 1234
- dimethoxymethane
- dimethyl formal
- formaldehyde, dimethyl acetal
- methanal, dimethyl acetal
- methylal
- ω : Acentric Factor.
- 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).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- 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 | [0.2222; 0.2856] |
|
|
| ω | 0.2222 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2856 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°gas | -1975.70 ± 0.75 | kJ/mol | NIST |
| μ | 0.74 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -226.30 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-348.20; -348.20] | kJ/mol |
|
| ΔfH°gas | -348.20 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -348.20 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 5.90 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [28.89; 29.60] | kJ/mol |
|
| ΔvapH° | 29.60 | kJ/mol | NIST |
| ΔvapH° | 28.89 ± 0.21 | kJ/mol | NIST |
| ΔvapH° | 28.89 ± 0.21 | kJ/mol | NIST |
| IE | [9.70; 10.42] | eV |
|
| IE | 9.70 | eV | NIST |
| IE | 10.00 ± 0.05 | eV | NIST |
| IE | 10.42 | eV | NIST |
| IE | 10.20 | eV | NIST |
| IE | 10.29 | eV | NIST |
| log10WS | [0.48; 0.48] |
|
|
| log10WS | 0.48 | Aq. Solubility Prediction | |
| log10WS | 0.48 | Estimated Solubility | |
| logPoct/wat | 0.237 | Crippen Calculated Property | |
| McVol | 64.870 | ml/mol | McGowan Calculated Property |
| Pc | [3950.00; 3960.00] | kPa |
|
| Pc | 3960.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 3957.76 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3950.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3950.00 ± 70.92 | kPa | NIST |
| Ptriple | 1.13e-03 | kPa | ChemSep v8.3 pure component data Compiled value |
| ρc | 356.88 ± 29.68 | kg/m3 | NIST |
| Inp | [500.00; 511.00] |
|
|
| Inp | 500.00 | NIST | |
| Inp | 511.00 | NIST | |
| Inp | 508.00 | NIST | |
| Inp | 508.00 | NIST | |
| Inp | 505.00 | NIST | |
| Inp | 505.00 | NIST | |
| Inp | 511.00 | NIST | |
| Ip | 740.00 | NIST | |
| S°gas | 335.72 ± 0.62 | J/mol×K | NIST |
| S°liquid | 244.01 | J/mol×K | NIST |
| Tboil | [314.70; 315.65] | K |
|
| Tboil | 315.25 | K | Vapor-Liquid Equilibria for the Binary Systems of Dimethoxymethane with Some Fuel Oxygenates |
| Tboil | 315.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | Outlier 314.70 | K | NIST |
| Tboil | 315.65 ± 1.00 | K | NIST |
| Tboil | 315.50 ± 0.60 | K | NIST |
| Tboil | 315.15 ± 1.00 | K | NIST |
| Tboil | 315.45 ± 0.20 | K | NIST |
| Tboil | 315.30 ± 0.50 | K | NIST |
| Tboil | 315.15 ± 1.50 | K | NIST |
| Tboil | 315.50 ± 0.40 | K | NIST |
| Tboil | 315.45 ± 0.30 | K | NIST |
| Tboil | 315.50 ± 0.60 | K | NIST |
| Tc | [480.60; 496.80] | K |
|
| Tc | 488.90 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tc | 491.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 490.90 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 480.60 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 480.60 ± 1.00 | K | NIST |
| Tc | 488.40 ± 6.00 | K | NIST |
| Tc | 496.80 ± 10.00 | K | NIST |
| Tfus | [168.00; 168.35] | K |
|
| Tfus | 168.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 168.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 168.20 | K | Aq. Solubility Prediction |
| Tfus | 168.00 ± 2.00 | K | NIST |
| Tfus | 168.35 ± 0.50 | K | NIST |
| Tfus | 168.15 ± 0.40 | K | NIST |
| Tfus | 168.35 ± 0.30 | K | NIST |
| Ttriple | [168.01; 168.35] | K |
|
| Ttriple | 168.35 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 168.03 ± 0.05 | K | NIST |
| Ttriple | 168.01 ± 0.02 | K | NIST |
| Ttriple | 168.01 ± 0.02 | K | NIST |
| UQi | 2.72 | ChemSep v8.3 pure component data Compiled value | |
| URi | 2.96 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.213; 0.213] | m3/kmol |
|
| Vc | 0.213 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Vc | 0.213 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.213 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | [0.2070000; 0.2110000] |
|
|
| Zc | 0.2070000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value | |
| Zc | 0.2110000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.25 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 243.15 | 100.00 | 0.0006 |
| 243.15 | 4400.00 | 0.0007 |
| 243.15 | 9420.00 | 0.0007 |
| 243.15 | 14450.00 | 0.0007 |
| 243.15 | 19440.00 | 0.0007 |
| 253.15 | 100.00 | 0.0005 |
| 253.15 | 4420.00 | 0.0006 |
| 253.15 | 9410.00 | 0.0006 |
| 253.15 | 14450.00 | 0.0006 |
| 253.15 | 19440.00 | 0.0006 |
| 263.15 | 100.00 | 0.0005 |
| 263.15 | 4440.00 | 0.0005 |
| 263.15 | 9440.00 | 0.0005 |
| 263.15 | 14470.00 | 0.0005 |
| 263.15 | 19470.00 | 0.0005 |
| 273.15 | 100.00 | 0.0004 |
| 273.15 | 4440.00 | 0.0004 |
| 273.15 | 9440.00 | 0.0004 |
| 273.15 | 14480.00 | 0.0005 |
| 273.15 | 19540.00 | 0.0005 |
| 283.15 | 100.00 | 0.0004 |
| 283.15 | 4450.00 | 0.0004 |
| 283.15 | 9430.00 | 0.0004 |
| 283.15 | 14490.00 | 0.0004 |
| 283.15 | 19550.00 | 0.0004 |
| 293.15 | 100.00 | 0.0003 |
| 293.15 | 4410.00 | 0.0003 |
| 293.15 | 9460.00 | 0.0004 |
| 293.15 | 14490.00 | 0.0004 |
| 293.15 | 19550.00 | 0.0004 |
| 303.15 | 100.00 | 0.0003 |
| 303.15 | 4450.00 | 0.0003 |
| 303.15 | 9450.00 | 0.0003 |
| 303.15 | 14490.00 | 0.0003 |
| 303.15 | 19550.00 | 0.0003 |
| 313.15 | 160.00 | 0.0003 |
| 313.15 | 4440.00 | 0.0003 |
| 313.15 | 9420.00 | 0.0003 |
| 313.15 | 14450.00 | 0.0003 |
| 313.15 | 19440.00 | 0.0003 |
| 323.15 | 190.00 | 0.0002 |
| 323.15 | 4390.00 | 0.0003 |
| 323.15 | 9420.00 | 0.0003 |
| 323.15 | 14460.00 | 0.0003 |
| 323.15 | 19490.00 | 0.0003 |
| 333.15 | 210.00 | 0.0002 |
| 333.15 | 4390.00 | 0.0002 |
| 333.15 | 9410.00 | 0.0002 |
| 333.15 | 14450.00 | 0.0003 |
| 333.15 | 19450.00 | 0.0003 |
| 343.15 | 280.00 | 0.0002 |
| 343.15 | 4430.00 | 0.0002 |
| 343.15 | 9430.00 | 0.0002 |
| 343.15 | 14460.00 | 0.0002 |
| 343.15 | 19460.00 | 0.0002 |
| 353.15 | 360.00 | 0.0002 |
| 353.15 | 4370.00 | 0.0002 |
| 353.15 | 9400.00 | 0.0002 |
| 353.15 | 14450.00 | 0.0002 |
| 353.15 | 19430.00 | 0.0002 |
| 363.15 | 430.00 | 0.0002 |
| 363.15 | 4400.00 | 0.0002 |
| 363.15 | 9410.00 | 0.0002 |
| 363.15 | 14450.00 | 0.0002 |
| 363.15 | 19460.00 | 0.0002 |
| 373.15 | 550.00 | 0.0002 |
| 373.15 | 4370.00 | 0.0002 |
| 373.15 | 9400.00 | 0.0002 |
| 373.15 | 14450.00 | 0.0002 |
| 373.15 | 19480.00 | 0.0002 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [74.37; 207.95] | J/mol×K | [168.35; 1000.15] |
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 | 7.33870e+01 | |||
| Coefficient B | -1.24900e+03 | |||
| Coefficient C | 7.86624e+00 | |||
| Coefficient D | -2.95520e-03 | |||
| Coefficient E | 1.23990e-06 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 1000.15 | |||
| Cp,gas | 74.37 | J/mol×K | 168.35 | Calculated Property |
| Cp,gas | 84.30 | J/mol×K | 260.77 | Calculated Property |
| Cp,gas | 104.60 | J/mol×K | 353.19 | Calculated Property |
| Cp,gas | 127.59 | J/mol×K | 445.62 | Calculated Property |
| Cp,gas | 148.11 | J/mol×K | 538.04 | Calculated Property |
| Cp,gas | 164.75 | J/mol×K | 630.46 | Calculated Property |
| Cp,gas | 177.98 | J/mol×K | 722.88 | Calculated Property |
| Cp,gas | 188.87 | J/mol×K | 815.31 | Calculated Property |
| Cp,gas | 198.52 | J/mol×K | 907.73 | Calculated Property |
| Cp,gas | 207.95 | J/mol×K | 1000.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [144.14; 165.79] | J/mol×K | [168.35; 315.00] |
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 | 1.34330e+02 | |||
| Coefficient B | 5.75020e+02 | |||
| Coefficient C | -6.17362e+00 | |||
| Coefficient D | 3.59060e-02 | |||
| Coefficient E | -3.54100e-05 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 315.00 | |||
| Cp,liquid | 144.14 | J/mol×K | 168.35 | Calculated Property |
| Cp,liquid | 144.95 | J/mol×K | 184.64 | Calculated Property |
| Cp,liquid | 146.19 | J/mol×K | 200.94 | Calculated Property |
| Cp,liquid | 147.83 | J/mol×K | 217.23 | Calculated Property |
| Cp,liquid | 149.86 | J/mol×K | 233.53 | Calculated Property |
| Cp,liquid | 152.29 | J/mol×K | 249.82 | Calculated Property |
| Cp,liquid | 155.12 | J/mol×K | 266.12 | Calculated Property |
| Cp,liquid | 158.34 | J/mol×K | 282.41 | Calculated Property |
| Cp,liquid | 161.92 | J/mol×K | 298.71 | Calculated Property |
| Cp,liquid | 165.79 | J/mol×K | 315.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0025222; 0.0001253] | Pa×s | [168.35; 450.00] |
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 | -8.40580e+00 | |||
| Coefficient B | 7.22360e+02 | |||
| Coefficient C | -3.65720e-01 | |||
| Coefficient D | 2.48190e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 450.00 | |||
| η | 0.0025222 | Pa×s | 168.35 | Calculated Property |
| η | 0.0012129 | Pa×s | 199.64 | Calculated Property |
| η | 0.0007067 | Pa×s | 230.94 | Calculated Property |
| η | 0.0004662 | Pa×s | 262.23 | Calculated Property |
| η | 0.0003350 | Pa×s | 293.53 | Calculated Property |
| η | 0.0002559 | Pa×s | 324.82 | Calculated Property |
| η | 0.0002046 | Pa×s | 356.12 | Calculated Property |
| η | 0.0001694 | Pa×s | 387.41 | Calculated Property |
| η | 0.0001441 | Pa×s | 418.71 | Calculated Property |
| η | 0.0001253 | Pa×s | 450.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [38.10; 0.00] | kJ/mol | [168.35; 480.60] |
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 | 4.95624e+01 | |||
| Coefficient B | 5.17705e-01 | |||
| Coefficient C | 7.08214e-01 | |||
| Coefficient D | -1.53026e+00 | |||
| Coefficient E | 7.44705e-01 | |||
| Critical temperature, Tc (K) | 4.80600e+02 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 480.60 | |||
| ΔvapH | 38.10 | kJ/mol | 168.35 | Calculated Property |
| ΔvapH | 35.65 | kJ/mol | 203.04 | Calculated Property |
| ΔvapH | 33.28 | kJ/mol | 237.74 | Calculated Property |
| ΔvapH | 30.94 | kJ/mol | 272.43 | Calculated Property |
| ΔvapH | 28.60 | kJ/mol | 307.13 | Calculated Property |
| ΔvapH | 26.13 | kJ/mol | 341.82 | Calculated Property |
| ΔvapH | 23.37 | kJ/mol | 376.52 | Calculated Property |
| ΔvapH | 19.96 | kJ/mol | 411.21 | Calculated Property |
| ΔvapH | 15.10 | kJ/mol | 445.91 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 480.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.80e-03; 3816.13] | kPa | [168.35; 480.60] |
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 | 5.52428e+01 | |||
| Coefficient B | -5.21794e+03 | |||
| Coefficient C | -5.98298e+00 | |||
| Coefficient D | 3.49124e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 480.60 | |||
| Pvap | 1.80e-03 | kPa | 168.35 | Calculated Property |
| Pvap | 0.12 | kPa | 203.04 | Calculated Property |
| Pvap | 2.13 | kPa | 237.74 | Calculated Property |
| Pvap | 16.44 | kPa | 272.43 | Calculated Property |
| Pvap | 74.93 | kPa | 307.13 | Calculated Property |
| Pvap | 239.67 | kPa | 341.82 | Calculated Property |
| Pvap | 598.54 | kPa | 376.52 | Calculated Property |
| Pvap | 1251.13 | kPa | 411.21 | Calculated Property |
| Pvap | 2294.58 | kPa | 445.91 | Calculated Property |
| Pvap | 3816.13 | kPa | 480.60 | Calculated Property |
| Pvap | [1.93e-03; 3888.46] | kPa | [168.35; 480.60] |
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 | 6.23348e+01 | |||
| Coefficient B | -5.39408e+03 | |||
| Coefficient C | -7.16190e+00 | |||
| Coefficient D | 5.97290e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 480.60 | |||
| Pvap | 1.93e-03 | kPa | 168.35 | Calculated Property |
| Pvap | 0.13 | kPa | 203.04 | Calculated Property |
| Pvap | 2.22 | kPa | 237.74 | Calculated Property |
| Pvap | 16.76 | kPa | 272.43 | Calculated Property |
| Pvap | 74.97 | kPa | 307.13 | Calculated Property |
| Pvap | 236.92 | kPa | 341.82 | Calculated Property |
| Pvap | 588.93 | kPa | 376.52 | Calculated Property |
| Pvap | 1235.20 | kPa | 411.21 | Calculated Property |
| Pvap | 2291.87 | kPa | 445.91 | Calculated Property |
| Pvap | 3888.46 | kPa | 480.60 | Calculated Property |
| Pvap | [17.26; 77.50] | kPa | [273.00; 308.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39001e+01 | |||
| Coefficient B | -2.45997e+03 | |||
| Coefficient C | -5.04090e+01 | |||
| Reference | Nicolini and Laffitte, 1949, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 308.00 | |||
| Pvap | 17.26 | kPa | 273.00 | Calculated Property |
| Pvap | 20.87 | kPa | 276.89 | Calculated Property |
| Pvap | 25.07 | kPa | 280.78 | Calculated Property |
| Pvap | 29.93 | kPa | 284.67 | Calculated Property |
| Pvap | 35.53 | kPa | 288.56 | Calculated Property |
| Pvap | 41.95 | kPa | 292.44 | Calculated Property |
| Pvap | 49.26 | kPa | 296.33 | Calculated Property |
| Pvap | 57.56 | kPa | 300.22 | Calculated Property |
| Pvap | 66.94 | kPa | 304.11 | Calculated Property |
| Pvap | 77.50 | kPa | 308.00 | Calculated Property |
| Pvap | [17.26; 77.50] | kPa | [273.00; 308.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39001e+01 | |||
| Coefficient B | -2.45997e+03 | |||
| Coefficient C | -5.04090e+01 | |||
| Reference | Nicolini and Laffitte, 1949 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 308.00 | |||
| Pvap | 17.26 | kPa | 273.00 | Calculated Property |
| Pvap | 20.87 | kPa | 276.89 | Calculated Property |
| Pvap | 25.07 | kPa | 280.78 | Calculated Property |
| Pvap | 29.93 | kPa | 284.67 | Calculated Property |
| Pvap | 35.53 | kPa | 288.56 | Calculated Property |
| Pvap | 41.95 | kPa | 292.44 | Calculated Property |
| Pvap | 49.26 | kPa | 296.33 | Calculated Property |
| Pvap | 57.56 | kPa | 300.22 | Calculated Property |
| Pvap | 66.94 | kPa | 304.11 | Calculated Property |
| Pvap | 77.50 | kPa | 308.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1004.04; 357.20] | kg/m3 | [168.35; 480.60] |
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 | 1.09203e+02 | |||
| Coefficient B | 3.05720e-01 | |||
| Coefficient C | 4.80600e+02 | |||
| Coefficient D | 3.17390e-01 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 480.60 | |||
| ρl | 1004.04 | kg/m3 | 168.35 | Calculated Property |
| ρl | 966.68 | kg/m3 | 203.04 | Calculated Property |
| ρl | 927.56 | kg/m3 | 237.74 | Calculated Property |
| ρl | 886.24 | kg/m3 | 272.43 | Calculated Property |
| ρl | 842.10 | kg/m3 | 307.13 | Calculated Property |
| ρl | 794.14 | kg/m3 | 341.82 | Calculated Property |
| ρl | 740.66 | kg/m3 | 376.52 | Calculated Property |
| ρl | 678.23 | kg/m3 | 411.21 | Calculated Property |
| ρl | 597.56 | kg/m3 | 445.91 | Calculated Property |
| ρl | 357.20 | kg/m3 | 480.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.02] | N/m | [168.35; 315.15] |
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 | 5.63407e-02 | |||
| Coefficient B | -1.19900e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 315.15 | |||
| γ | 0.04 | N/m | 168.35 | Calculated Property |
| γ | 0.03 | N/m | 184.66 | Calculated Property |
| γ | 0.03 | N/m | 200.97 | Calculated Property |
| γ | 0.03 | N/m | 217.28 | Calculated Property |
| γ | 0.03 | N/m | 233.59 | Calculated Property |
| γ | 0.03 | N/m | 249.91 | Calculated Property |
| γ | 0.02 | N/m | 266.22 | Calculated Property |
| γ | 0.02 | N/m | 282.53 | Calculated Property |
| γ | 0.02 | N/m | 298.84 | Calculated Property |
| γ | 0.02 | N/m | 315.15 | Calculated Property |
| γ | [0.04; 2.20e-05] | N/m | [168.35; 475.92] |
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 | -2.73960e-02 | |||
| Coefficient B | -6.20540e+00 | |||
| Coefficient C | -2.24510e+00 | |||
| Coefficient D | -2.21040e-03 | |||
| Coefficient E | -1.26470e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 480.6 K. | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 475.92 | |||
| γ | 0.04 | N/m | 168.35 | Calculated Property |
| γ | 0.03 | N/m | 202.52 | Calculated Property |
| γ | 0.03 | N/m | 236.70 | Calculated Property |
| γ | 0.02 | N/m | 270.87 | Calculated Property |
| γ | 0.02 | N/m | 305.05 | Calculated Property |
| γ | 0.02 | N/m | 339.22 | Calculated Property |
| γ | 0.01 | N/m | 373.39 | Calculated Property |
| γ | 0.01 | N/m | 407.57 | Calculated Property |
| γ | 0.00 | N/m | 441.74 | Calculated Property |
| γ | 2.20e-05 | N/m | 475.92 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.08] | W/m×K | [168.35; 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 | 1.48690e-03 | |||
| Coefficient B | 6.58460e-01 | |||
| Coefficient C | 4.70640e+02 | |||
| Coefficient D | 2.06460e+05 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 168.35 | Calculated Property |
| λgas | 0.01 | W/m×K | 260.76 | Calculated Property |
| λgas | 0.02 | W/m×K | 353.16 | Calculated Property |
| λgas | 0.03 | W/m×K | 445.57 | Calculated Property |
| λgas | 0.04 | W/m×K | 537.97 | Calculated Property |
| λgas | 0.05 | W/m×K | 630.38 | Calculated Property |
| λgas | 0.06 | W/m×K | 722.78 | Calculated Property |
| λgas | 0.07 | W/m×K | 815.19 | Calculated Property |
| λgas | 0.07 | W/m×K | 907.59 | Calculated Property |
| λgas | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.19; 0.14] | W/m×K | [168.35; 315.00] |
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 | 1.15430e-01 | |||
| Coefficient B | -7.76650e+02 | |||
| Coefficient C | 7.88200e+00 | |||
| Coefficient D | -4.12060e-02 | |||
| Coefficient E | 3.81210e-05 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 315.00 | |||
| λliquid | 0.19 | W/m×K | 168.35 | Calculated Property |
| λliquid | 0.19 | W/m×K | 184.64 | Calculated Property |
| λliquid | 0.18 | W/m×K | 200.94 | Calculated Property |
| λliquid | 0.17 | W/m×K | 217.23 | Calculated Property |
| λliquid | 0.17 | W/m×K | 233.53 | Calculated Property |
| λliquid | 0.16 | W/m×K | 249.82 | Calculated Property |
| λliquid | 0.15 | W/m×K | 266.12 | Calculated Property |
| λliquid | 0.15 | W/m×K | 282.41 | Calculated Property |
| λliquid | 0.14 | W/m×K | 298.71 | Calculated Property |
| λliquid | 0.14 | W/m×K | 315.00 | Calculated Property |
Similar Compounds
![Ethane, 1,1'-[methylenebis(oxy)]bis-.](data:image/png;base64,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)
Find more compounds similar to Methane, dimethoxy-.
Mixtures
- Methane, dimethoxy- + Water
- Methane, dimethoxy- + Ethanol, 2,2'-oxybis- + Water
- Methyl formate + Methane, dimethoxy-
- Carbonic acid, dimethyl ester + Methane, dimethoxy-
- p-Xylene + Methane, dimethoxy- + Water
- Methane, dimethoxy- + Methyl Alcohol
- 1,2-Ethanediol + Methane, dimethoxy- + Methyl Alcohol
- Methane, dimethoxy- + Pentane, 2,2,4-trimethyl-
- Methane, dimethoxy- + Cyclohexane + Water
- Methane, dimethoxy- + Heptane + Water
- Toluene + Methane, dimethoxy- + Water
- 2-Pentanol, 4-methyl- + Methane, dimethoxy- + Water
- Methane, dimethoxy- + o-Xylene + Water
- Methane, dimethoxy- + Propane, 2-methoxy-2-methyl-
- Diisopropyl ether + Methane, dimethoxy-
- 2-Propanol + Methane, dimethoxy-
- n-Hexane + Methane, dimethoxy-
- Methane, dimethoxy- + Cyclohexane
- Benzene + Methane, dimethoxy-
- sodium formate + Methane, dimethoxy- + Water
Find more mixtures with Methane, dimethoxy-.
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).
- 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.
- 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
- Density and Viscosity Measurements of Dimethoxymethane and 1,2-Dimethoxyethane from 243 K to 373 K up to 20 MPa
- Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane
- Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
- Isobaric vapor-liquid equilibria for binary mixtures from methyl methanoate, dimethoxymethane and dimethyl carbonate at 101.33 kPa
- Liquid-liquid equilibrium in binary and ternary mixtures containing formaldehyde, water, methanol, methylal, and poly(oxymethylene) dimethyl ethers
- Extractive distillation of methylal/methanol mixture using ethylene glycol as entrainer
- Liquid-liquid equilibria for ternary systems polyoxymethylene dimethyl ethers + para-xylene + water
- Extraction of Low Concentration Aqueous Solution of Methylal: Liquid Liquid Equilibrium in Water + Methylal + (Cyclohexane and n-Heptane) Ternary Systems
- DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
- Measurement and Thermodynamic Models for Ternary Liquid-Liquid Equilibrium Systems {Water + Polyoxymethylene Dimethyl Ethers +4-Methyl-2-pentanol} at Different Temperatures
- Liquid-Liquid Equilibrium for Ternary Systems of Polyoxymethylene Dimethyl Ethers + o-Xylene + Water at 293.15 K
- Salting Effect of Sodium Hydroxide and Sodium Formate on the Liquid-Liquid Equilibrium of Polyoxymethylene Dimethyl Ethers in Aqueous Solution
- Experimental and Correlated Liquid-Liquid Equilibrium Data for Ternary Systems (Water + Poly(oxymethylene) Dimethyl Ethers + Toluene) at T = 293.15 and 303.15 K and p = 101.3 kPa
- Vapor-Liquid Equilibria for the Binary Systems of Dimethoxymethane with Some Fuel Oxygenates
- Density and Viscosity of Saturated Liquid Dimethoxymethane from (218.15 to 383.15) K
- Vapor-Liquid Equilibria and Excess Enthalpies for Binary Systems of Dimethoxymethane with Hydrocarbons
- Vapor Pressure of Dimethoxymethane and 1,1,1,3,3-Pentafluoropropane
- Surface Tension of Dimethoxymethane and Methyl tert-Butyl Ether
- Refined Flow Microcalorimetric Setup for Measurement of Mixing Enthalpies at High Dilutions: Determination of Infinite Dilution Dissolution Enthalpies of Some Alkanol and Ether Solutes in Water
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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