- 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
- Dimethoxymethane
- Dimethyl formal
- Dimethylacetal formaldehyde
- Formal
- Formaldehyde dimethyl acetal
- Formaldehyde methyl ketal
- Methane, dimethoxy-
- Methoxymethyl methyl ether
- Methylene dimethyl ether
- Methylene glycol dimethylether
- Methylenedioxydimethane
- Metylal
- UN 1234
- formaldehyde, dimethyl acetal
- methanal, dimethyl acetal
- 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).
- 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).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : 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).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°gas | -1975.70 ± 0.75 | kJ/mol | NIST |
| ΔfG° | -235.62 | kJ/mol | Joback Calculated Property |
| 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 |
| 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. Sol... | |
| log10WS | 0.48 | Estimat... | |
| logPoct/wat | 0.237 | Crippen Calculated Property | |
| McVol | 64.870 | ml/mol | McGowan Calculated Property |
| Pc | 3950.00 ± 70.92 | kPa | NIST |
| 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 | |
| I | 740.00 | NIST | |
| S°gas | 335.72 ± 0.62 | J/mol×K | NIST |
| S°liquid | 244.01 | J/mol×K | NIST |
| Tboil | 315.25 | K | Vapor-L... |
| Tc | [480.60; 496.80] | K |
|
| 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 | 168.20 | K | Aq. Sol... |
| 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; 168.03] | K |
|
| Ttriple | 168.03 ± 0.05 | K | NIST |
| Ttriple | 168.01 ± 0.02 | K | NIST |
| Vc | 0.239 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [107.46; 138.28] | J/mol×K | [312.88; 477.41] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 105 110 115 120 125 130 135 140 350 400 450 | ||||
| Cp,gas | 107.46 | J/mol×K | 312.88 | Joback Calculated Property |
| Cp,gas | 112.65 | J/mol×K | 340.30 | Joback Calculated Property |
| Cp,gas | 117.83 | J/mol×K | 367.72 | Joback Calculated Property |
| Cp,gas | 123.00 | J/mol×K | 395.15 | Joback Calculated Property |
| Cp,gas | 128.13 | J/mol×K | 422.57 | Joback Calculated Property |
| Cp,gas | 133.23 | J/mol×K | 449.99 | Joback Calculated Property |
| Cp,gas | 138.28 | J/mol×K | 477.41 | Joback Calculated Property |
| Cp,liquid | [161.42; 163.60] | J/mol×K | [298.00; 298.15] |
|
| Cp,liquid | 163.60 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 161.42 | J/mol×K | 298.15 | NIST |
| η | [0.0001420; 0.0012631] | Pa×s | [218.09; 383.16] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 250 300 350 | ||||
| η | 0.0012630 | Pa×s | 218.09 | Density... |
| η | 0.0012631 | Pa×s | 218.09 | Density... |
| η | 0.0010987 | Pa×s | 223.09 | Density... |
| η | 0.0010987 | Pa×s | 223.09 | Density... |
| η | 0.0009649 | Pa×s | 228.10 | Density... |
| η | 0.0009648 | Pa×s | 228.11 | Density... |
| η | 0.0008557 | Pa×s | 233.10 | Density... |
| η | 0.0008556 | Pa×s | 233.10 | Density... |
| η | 0.0007648 | Pa×s | 238.11 | Density... |
| η | 0.0007648 | Pa×s | 238.11 | Density... |
| η | 0.0006886 | Pa×s | 243.14 | Density... |
| η | 0.0006885 | Pa×s | 243.15 | Density... |
| η | 0.0006248 | Pa×s | 248.14 | Density... |
| η | 0.0006248 | Pa×s | 248.14 | Density... |
| η | 0.0005705 | Pa×s | 253.13 | Density... |
| η | 0.0005705 | Pa×s | 253.14 | Density... |
| η | 0.0005240 | Pa×s | 258.12 | Density... |
| η | 0.0005238 | Pa×s | 258.15 | Density... |
| η | 0.0004841 | Pa×s | 263.07 | Density... |
| η | 0.0004839 | Pa×s | 263.09 | Density... |
| η | 0.0004489 | Pa×s | 268.09 | Density... |
| η | 0.0004489 | Pa×s | 268.09 | Density... |
| η | 0.0004183 | Pa×s | 273.05 | Density... |
| η | 0.0004183 | Pa×s | 273.05 | Density... |
| η | 0.0003912 | Pa×s | 278.05 | Density... |
| η | 0.0003912 | Pa×s | 278.05 | Density... |
| η | 0.0003669 | Pa×s | 283.10 | Density... |
| η | 0.0003669 | Pa×s | 283.10 | Density... |
| η | 0.0003452 | Pa×s | 288.17 | Density... |
| η | 0.0003451 | Pa×s | 288.17 | Density... |
| η | 0.0003262 | Pa×s | 293.09 | Density... |
| η | 0.0003262 | Pa×s | 293.09 | Density... |
| η | 0.0003086 | Pa×s | 298.12 | Density... |
| η | 0.0003086 | Pa×s | 298.13 | Density... |
| η | 0.0002927 | Pa×s | 303.12 | Density... |
| η | 0.0002927 | Pa×s | 303.13 | Density... |
| η | 0.0002781 | Pa×s | 308.16 | Density... |
| η | 0.0002781 | Pa×s | 308.17 | Density... |
| η | 0.0002647 | Pa×s | 313.16 | Density... |
| η | 0.0002647 | Pa×s | 313.16 | Density... |
| η | 0.0002524 | Pa×s | 318.16 | Density... |
| η | 0.0002524 | Pa×s | 318.17 | Density... |
| η | 0.0002410 | Pa×s | 323.15 | Density... |
| η | 0.0002409 | Pa×s | 323.15 | Density... |
| η | 0.0002303 | Pa×s | 328.14 | Density... |
| η | 0.0002303 | Pa×s | 328.14 | Density... |
| η | 0.0002202 | Pa×s | 333.14 | Density... |
| η | 0.0002202 | Pa×s | 333.15 | Density... |
| η | 0.0002107 | Pa×s | 338.15 | Density... |
| η | 0.0002107 | Pa×s | 338.15 | Density... |
| η | 0.0002017 | Pa×s | 343.15 | Density... |
| η | 0.0002017 | Pa×s | 343.15 | Density... |
| η | 0.0001931 | Pa×s | 348.16 | Density... |
| η | 0.0001931 | Pa×s | 348.16 | Density... |
| η | 0.0001850 | Pa×s | 353.12 | Density... |
| η | 0.0001850 | Pa×s | 353.13 | Density... |
| η | 0.0001771 | Pa×s | 358.16 | Density... |
| η | 0.0001771 | Pa×s | 358.16 | Density... |
| η | 0.0001696 | Pa×s | 363.15 | Density... |
| η | 0.0001696 | Pa×s | 363.15 | Density... |
| η | 0.0001624 | Pa×s | 368.14 | Density... |
| η | 0.0001623 | Pa×s | 368.16 | Density... |
| η | 0.0001554 | Pa×s | 373.14 | Density... |
| η | 0.0001554 | Pa×s | 373.14 | Density... |
| η | 0.0001486 | Pa×s | 378.15 | Density... |
| η | 0.0001486 | Pa×s | 378.15 | Density... |
| η | 0.0001420 | Pa×s | 383.15 | Density... |
| η | 0.0001420 | Pa×s | 383.16 | Density... |
| ΔfusH | [8.33; 8.33] | kJ/mol | [168.00; 168.01] |
|
| ΔfusH | 8.33 | kJ/mol | 168.00 | NIST |
| ΔfusH | 8.33 | kJ/mol | 168.00 | NIST |
| ΔfusH | 8.33 | kJ/mol | 168.01 | NIST |
| ΔvapH | [28.89; 31.20] | kJ/mol | [290.50; 305.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 29 29.5 30 30.5 31 295 300 305 | ||||
| ΔvapH | 30.10 | kJ/mol | 290.50 | NIST |
| ΔvapH | 31.20 | kJ/mol | 294.50 | NIST |
| ΔvapH | 29.80 | kJ/mol | 295.50 | NIST |
| ΔvapH | 28.89 | kJ/mol | 298.15 | NIST |
| ΔvapH | 30.30 | kJ/mol | 305.00 | NIST |
| Pvap | [27.73; 935.48] | kPa | [283.13; 398.15] |
|
|
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 300 350 400 | ||||
| Pvap | 27.73 | kPa | 283.13 | Vapor P... |
| Pvap | 30.39 | kPa | 285.13 | Vapor P... |
| Pvap | 34.73 | kPa | 288.11 | Vapor P... |
| Pvap | 43.08 | kPa | 293.07 | Vapor P... |
| Pvap | 46.83 | kPa | 295.07 | Vapor P... |
| Pvap | 52.94 | kPa | 298.07 | Vapor P... |
| Pvap | 57.14 | kPa | 300.07 | Vapor P... |
| Pvap | 64.26 | kPa | 303.05 | Vapor P... |
| Pvap | 69.42 | kPa | 305.05 | Vapor P... |
| Pvap | 77.74 | kPa | 308.05 | Vapor P... |
| Pvap | 83.80 | kPa | 310.07 | Vapor P... |
| Pvap | 93.85 | kPa | 313.16 | Vapor P... |
| Pvap | 111.95 | kPa | 318.13 | Vapor P... |
| Pvap | 132.98 | kPa | 323.17 | Vapor P... |
| Pvap | 142.06 | kPa | 325.18 | Vapor P... |
| Pvap | 156.44 | kPa | 328.17 | Vapor P... |
| Pvap | 166.67 | kPa | 330.17 | Vapor P... |
| Pvap | 182.96 | kPa | 333.17 | Vapor P... |
| Pvap | 194.47 | kPa | 335.17 | Vapor P... |
| Pvap | 212.79 | kPa | 338.16 | Vapor P... |
| Pvap | 225.73 | kPa | 340.16 | Vapor P... |
| Pvap | 246.24 | kPa | 343.16 | Vapor P... |
| Pvap | 260.68 | kPa | 345.16 | Vapor P... |
| Pvap | 283.65 | kPa | 348.16 | Vapor P... |
| Pvap | 325.16 | kPa | 353.16 | Vapor P... |
| Pvap | 371.53 | kPa | 358.16 | Vapor P... |
| Pvap | 421.82 | kPa | 363.16 | Vapor P... |
| Pvap | 477.61 | kPa | 368.16 | Vapor P... |
| Pvap | 538.51 | kPa | 373.15 | Vapor P... |
| Pvap | 605.33 | kPa | 378.16 | Vapor P... |
| Pvap | 677.68 | kPa | 383.13 | Vapor P... |
| Pvap | 757.05 | kPa | 388.15 | Vapor P... |
| Pvap | 842.82 | kPa | 393.16 | Vapor P... |
| Pvap | 935.48 | kPa | 398.15 | Vapor P... |
| ρl | [847.51; 848.59] | kg/m3 | [298.15; 303.15] |
|
| ρl | 847.51 | kg/m3 | 298.15 | Phase e... |
| ρl | 847.51 | kg/m3 | 298.15 | Vapor-L... |
| ρl | 848.59 | kg/m3 | 303.15 | Isobari... |
| ΔfusS | 49.59 | J/mol×K | 168.01 | NIST |
| γ | [0.01; 0.03] | N/m | [238.07; 388.14] |
|
|
T(K) Surface Tension (N/m) 0.01 0.02 0.02 0.03 0.03 250 300 350 | ||||
| γ | 0.03 | N/m | 238.07 | Surface... |
| γ | 0.03 | N/m | 243.12 | Surface... |
| γ | 0.03 | N/m | 248.13 | Surface... |
| γ | 0.03 | N/m | 253.12 | Surface... |
| γ | 0.03 | N/m | 258.12 | Surface... |
| γ | 0.02 | N/m | 263.08 | Surface... |
| γ | 0.02 | N/m | 268.09 | Surface... |
| γ | 0.02 | N/m | 273.09 | Surface... |
| γ | 0.02 | N/m | 278.08 | Surface... |
| γ | 0.02 | N/m | 283.07 | Surface... |
| γ | 0.02 | N/m | 288.08 | Surface... |
| γ | 0.02 | N/m | 293.05 | Surface... |
| γ | 0.02 | N/m | 298.04 | Surface... |
| γ | 0.02 | N/m | 303.16 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 313.16 | Surface... |
| γ | 0.02 | N/m | 318.16 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
| γ | 0.02 | N/m | 328.13 | Surface... |
| γ | 0.02 | N/m | 333.16 | Surface... |
| γ | 0.02 | N/m | 338.16 | Surface... |
| γ | 0.01 | N/m | 343.15 | Surface... |
| γ | 0.01 | N/m | 348.14 | Surface... |
| γ | 0.01 | N/m | 353.15 | Surface... |
| γ | 0.01 | N/m | 358.15 | Surface... |
| γ | 0.01 | N/m | 363.15 | Surface... |
| γ | 0.01 | N/m | 368.15 | Surface... |
| γ | 0.01 | N/m | 373.15 | Surface... |
| γ | 0.01 | N/m | 378.15 | Surface... |
| γ | 0.01 | N/m | 383.13 | Surface... |
| γ | 0.01 | N/m | 388.14 | Surface... |
| ΔvapS | 96.90 | J/mol×K | 298.15 | NIST |
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 |
|---|---|---|---|---|
| Pvap | [1.93e-03; 3888.46] | kPa | [168.35; 480.60] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.23348e+01 | |||
| Coefficient B | -5.39408e+03 | |||
| Coefficient C | -7.16190e+00 | |||
| Coefficient D | 5.97290e-06 | |||
| Temperature range, min. | 168.35 | |||
| Temperature range, max. | 480.60 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 | ||||
| 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 |
Similar Compounds
Find more compounds similar to Methylal.
Mixtures
- Methylal + Pentane, 2,2,4-trimethyl-
- Methyl formate + Methylal
- Carbonic acid, dimethyl ester + Methylal
- Methylal + Propane, 2-methoxy-2-methyl-
- Diisopropyl ether + Methylal
- Isopropyl Alcohol + Methylal
- n-Hexane + Methylal
- Methylal + Cyclohexane
- Benzene + Methylal
- Methylal + Water
- Methylal + Methyl Alcohol
- 1,2-Ethanediol + Methylal + Methyl Alcohol
- Methylal + Ethanol, 2,2'-oxybis- + Water
- p-Xylene + Methylal + Water
- Methylal + Cyclohexane + Water
- Methylal + Heptane + Water
- 2-Pentanol, 4-methyl- + Methylal + Water
- Methylal + o-Xylene + Water
- sodium formate + Methylal + Water
- sodium hydroxide + Methylal + Water
Find more mixtures with Methylal.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- 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
- 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
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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