- InChI
- InChI=1S/C6H14O3/c1-7-3-5-9-6-4-8-2/h3-6H2,1-2H3
- InChI Key
- SBZXBUIDTXKZTM-UHFFFAOYSA-N
- Formula
- C6H14O3
- SMILES
- COCCOCCOC
- Molecular Weight1
- 134.17
- CAS
- 111-96-6
- Other Names
-
- (2-Methoxyethyl) ether
- .beta.,.beta.-dimethoxy diethyl ether
- 1,1'-Oxybis(2-methoxy)ethane
- 1,1'-oxybis(2-methoxyethane)
- 1,5-dimethoxydiethyl ether
- 2,2'-Oxybisethanol dimethyl ether
- 2,5,8-Trioxanonane
- 2-(2-Methoxyethoxy)-1-methoxyethane
- 2-methoxyethyl ether
- 3-oxa-1,5-pentanediol, dimethyl ether
- Bis(2-methoxyethyl) ether
- CH3OCH2CH2OCH2CH2OCH3
- Di(2-Methoxyethyl) ether
- Diethyl glycol dimethyl ether
- Diethylene glycol dimethyl ether
- Diglycol methyl ether
- Diglyme
- Dimethoxydiethylene glycol
- Dimethyl carbitol
- Dimethyldigol
- Ethanol, 2,2'-oxybis-, dimethyl ether
- Ether, bis(2-methoxyethyl)
- Glyme-2
- Methyl diglyme
- NSC 59726
- Poly-Solv
- diethylene glycol, dimethyl ether
- diglyme (diethylene glycol dimethyl ether)
- dimethyldiglycol
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- 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).
- 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).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 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 |
|---|---|---|---|
| PAff | 918.80 | kJ/mol | NIST |
| BasG | 870.90 | kJ/mol | NIST |
| ΔcH°liquid | -3805.50 ± 0.90 | kJ/mol | NIST |
| ΔfG° | -315.36 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-524.70; -511.70] | kJ/mol |
|
| ΔfH°gas | -511.70 | kJ/mol | NIST |
| ΔfH°gas | -524.70 | kJ/mol | NIST |
| ΔfH°liquid | [-569.40; -556.40] | kJ/mol |
|
| ΔfH°liquid | -556.40 ± 0.90 | kJ/mol | NIST |
| ΔfH°liquid | -569.40 | kJ/mol | NIST |
| ΔfusH° | 14.86 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [44.70; 48.00] | kJ/mol |
|
| ΔvapH° | 48.00 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 44.70 | kJ/mol | NIST |
| IE | 9.80 | eV | NIST |
| log10WS | 0.88 | Aq. Sol... | |
| logPoct/wat | 0.296 | Crippen Calculated Property | |
| McVol | 113.010 | ml/mol | McGowan Calculated Property |
| Pc | 2937.70 | kPa | Joback Calculated Property |
| Inp | [950.90; 951.00] |
|
|
| Inp | 951.00 | NIST | |
| Inp | 950.90 | NIST | |
| Inp | 950.90 | NIST | |
| S°liquid | 352.70 | J/mol×K | NIST |
| Tboil | [435.00; 435.20] | K |
|
| Tboil | 435.20 | K | NIST |
| Tboil | 435.15 | K | NIST |
| Tboil | 435.00 ± 4.00 | K | NIST |
| Tc | 569.71 | K | Joback Calculated Property |
| Tfus | [207.82; 209.15] | K |
|
| Tfus | 207.82 | K | Aq. Sol... |
| Tfus | 209.15 | K | NIST |
| Tfus | 209.10 ± 0.20 | K | NIST |
| Vc | 0.425 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [227.24; 283.44] | J/mol×K | [403.94; 569.71] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 230 240 250 260 270 280 400 450 500 550 | ||||
| Cp,gas | 227.24 | J/mol×K | 403.94 | Joback Calculated Property |
| Cp,gas | 237.05 | J/mol×K | 431.57 | Joback Calculated Property |
| Cp,gas | 246.70 | J/mol×K | 459.20 | Joback Calculated Property |
| Cp,gas | 256.17 | J/mol×K | 486.83 | Joback Calculated Property |
| Cp,gas | 265.47 | J/mol×K | 514.45 | Joback Calculated Property |
| Cp,gas | 274.56 | J/mol×K | 542.08 | Joback Calculated Property |
| Cp,gas | 283.44 | J/mol×K | 569.71 | Joback Calculated Property |
| Cp,liquid | [274.10; 279.84] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 277.76 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 279.84 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 274.10 | J/mol×K | 298.15 | NIST |
| η | [0.0004120; 0.0015200] | Pa×s | [273.15; 363.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 300 350 | ||||
| η | 0.0015200 | Pa×s | 273.15 | Density... |
| η | 0.0013800 | Pa×s | 278.15 | Density... |
| η | 0.0012600 | Pa×s | 283.15 | Density... |
| η | 0.0011400 | Pa×s | 288.15 | Density... |
| η | 0.0010600 | Pa×s | 293.15 | Density... |
| η | 0.0009760 | Pa×s | 298.15 | Density... |
| η | 0.0009010 | Pa×s | 303.15 | Density... |
| η | 0.0007770 | Pa×s | 313.15 | Density... |
| η | 0.0006760 | Pa×s | 323.15 | Density... |
| η | 0.0005920 | Pa×s | 333.15 | Density... |
| η | 0.0005220 | Pa×s | 343.15 | Density... |
| η | 0.0004640 | Pa×s | 353.15 | Density... |
| η | 0.0004120 | Pa×s | 363.15 | Density... |
| ΔfusH | [17.78; 17.80] | kJ/mol | [209.10; 209.10] |
|
| ΔfusH | 17.78 | kJ/mol | 209.10 | NIST |
| ΔfusH | 17.80 | kJ/mol | 209.10 | NIST |
| ΔfusH | 17.80 | kJ/mol | 209.10 | NIST |
| ΔvapH | [45.40; 47.40] | kJ/mol | [359.50; 402.50] |
|
| ΔvapH | 47.40 | kJ/mol | 359.50 | NIST |
| ΔvapH | 45.40 | kJ/mol | 402.50 | NIST |
| n0 | [1.39680; 1.41010] | [288.15; 318.15] |
|
|
|
T(K) Refractive Index 1.4 1.4 1.4 1.4 1.4 1.41 1.41 1.41 290 300 310 | ||||
| n0 | 1.41010 | 288.15 | Liquid ... | |
| n0 | 1.40580 | 298.15 | Non-ide... | |
| n0 | 1.40580 | 298.15 | Liquid ... | |
| n0 | 1.40570 | 298.15 | Solubil... | |
| n0 | 1.40600 | 298.15 | Density... | |
| n0 | 1.40120 | 308.15 | Liquid ... | |
| n0 | 1.39680 | 318.15 | Liquid ... | |
| ρl | [863.80; 953.70] | kg/m3 | [283.15; 373.15] |
|
|
T(K) Liquid Density (kg/m3) 860 880 900 920 940 960 300 320 340 360 | ||||
| ρl | 953.70 | kg/m3 | 283.15 | Thermop... |
| ρl | 953.66 | kg/m3 | 283.15 | Volumet... |
| ρl | 952.67 | kg/m3 | 284.15 | Volumet... |
| ρl | 951.69 | kg/m3 | 285.15 | Volumet... |
| ρl | 950.70 | kg/m3 | 286.15 | Volumet... |
| ρl | 949.71 | kg/m3 | 287.15 | Volumet... |
| ρl | 948.70 | kg/m3 | 288.15 | Thermop... |
| ρl | 950.20 | kg/m3 | 288.15 | Thermop... |
| ρl | 948.72 | kg/m3 | 288.15 | Volumet... |
| ρl | 947.73 | kg/m3 | 289.15 | Volumet... |
| ρl | 946.74 | kg/m3 | 290.15 | Volumet... |
| ρl | 945.75 | kg/m3 | 291.15 | Volumet... |
| ρl | 944.76 | kg/m3 | 292.15 | Volumet... |
| ρl | 943.80 | kg/m3 | 293.15 | Thermop... |
| ρl | 945.20 | kg/m3 | 293.15 | Excess ... |
| ρl | 945.20 | kg/m3 | 293.15 | Thermop... |
| ρl | 943.76 | kg/m3 | 293.15 | Volumet... |
| ρl | 942.79 | kg/m3 | 294.15 | Volumet... |
| ρl | 941.79 | kg/m3 | 295.15 | Volumet... |
| ρl | 940.79 | kg/m3 | 296.15 | Volumet... |
| ρl | 939.80 | kg/m3 | 297.15 | Volumet... |
| ρl | 938.80 | kg/m3 | 298.15 | Thermop... |
| ρl | 938.80 | kg/m3 | 298.15 | Volumet... |
| ρl | 940.20 | kg/m3 | 298.15 | Thermop... |
| ρl | 939.80 | kg/m3 | 298.15 | Excess ... |
| ρl | 938.62 | kg/m3 | 298.15 | Excess ... |
| ρl | 937.80 | kg/m3 | 299.15 | Volumet... |
| ρl | 936.81 | kg/m3 | 300.15 | Volumet... |
| ρl | 935.81 | kg/m3 | 301.15 | Volumet... |
| ρl | 934.82 | kg/m3 | 302.15 | Volumet... |
| ρl | 933.80 | kg/m3 | 303.15 | Thermop... |
| ρl | 935.20 | kg/m3 | 303.15 | Thermop... |
| ρl | 935.00 | kg/m3 | 303.15 | Excess ... |
| ρl | 933.98 | kg/m3 | 303.15 | Surface... |
| ρl | 933.82 | kg/m3 | 303.15 | Volumet... |
| ρl | 932.82 | kg/m3 | 304.15 | Volumet... |
| ρl | 931.82 | kg/m3 | 305.15 | Volumet... |
| ρl | 930.82 | kg/m3 | 306.15 | Volumet... |
| ρl | 929.83 | kg/m3 | 307.15 | Volumet... |
| ρl | 928.80 | kg/m3 | 308.15 | Thermop... |
| ρl | 930.70 | kg/m3 | 308.15 | Excess ... |
| ρl | 930.20 | kg/m3 | 308.15 | Thermop... |
| ρl | 928.83 | kg/m3 | 308.15 | Volumet... |
| ρl | 928.95 | kg/m3 | 308.15 | Surface... |
| ρl | 927.82 | kg/m3 | 309.15 | Volumet... |
| ρl | 926.83 | kg/m3 | 310.15 | Volumet... |
| ρl | 925.82 | kg/m3 | 311.15 | Volumet... |
| ρl | 924.82 | kg/m3 | 312.15 | Volumet... |
| ρl | 923.80 | kg/m3 | 313.15 | Thermop... |
| ρl | 925.20 | kg/m3 | 313.15 | Thermop... |
| ρl | 923.97 | kg/m3 | 313.15 | Surface... |
| ρl | 925.40 | kg/m3 | 313.15 | Excess ... |
| ρl | 923.82 | kg/m3 | 313.15 | Volumet... |
| ρl | 922.81 | kg/m3 | 314.15 | Volumet... |
| ρl | 921.81 | kg/m3 | 315.15 | Volumet... |
| ρl | 920.80 | kg/m3 | 316.15 | Volumet... |
| ρl | 919.80 | kg/m3 | 317.15 | Volumet... |
| ρl | 920.20 | kg/m3 | 318.15 | Thermop... |
| ρl | 918.94 | kg/m3 | 318.15 | Surface... |
| ρl | 918.79 | kg/m3 | 318.15 | Volumet... |
| ρl | 917.78 | kg/m3 | 319.15 | Volumet... |
| ρl | 916.78 | kg/m3 | 320.15 | Volumet... |
| ρl | 915.77 | kg/m3 | 321.15 | Volumet... |
| ρl | 914.75 | kg/m3 | 322.15 | Volumet... |
| ρl | 913.90 | kg/m3 | 323.15 | Surface... |
| ρl | 913.70 | kg/m3 | 323.15 | Thermop... |
| ρl | 915.20 | kg/m3 | 323.15 | Thermop... |
| ρl | 913.75 | kg/m3 | 323.15 | Volumet... |
| ρl | 912.73 | kg/m3 | 324.15 | Volumet... |
| ρl | 911.72 | kg/m3 | 325.15 | Volumet... |
| ρl | 910.70 | kg/m3 | 326.15 | Volumet... |
| ρl | 909.69 | kg/m3 | 327.15 | Volumet... |
| ρl | 908.84 | kg/m3 | 328.15 | Surface... |
| ρl | 908.67 | kg/m3 | 328.15 | Volumet... |
| ρl | 910.10 | kg/m3 | 328.15 | Thermop... |
| ρl | 907.65 | kg/m3 | 329.15 | Volumet... |
| ρl | 906.63 | kg/m3 | 330.15 | Volumet... |
| ρl | 905.62 | kg/m3 | 331.15 | Volumet... |
| ρl | 904.60 | kg/m3 | 332.15 | Volumet... |
| ρl | 905.00 | kg/m3 | 333.15 | Thermop... |
| ρl | 903.76 | kg/m3 | 333.15 | Surface... |
| ρl | 903.60 | kg/m3 | 333.15 | Thermop... |
| ρl | 903.59 | kg/m3 | 333.15 | Volumet... |
| ρl | 898.67 | kg/m3 | 338.15 | Surface... |
| ρl | 899.90 | kg/m3 | 338.15 | Thermop... |
| ρl | 894.80 | kg/m3 | 343.15 | Thermop... |
| ρl | 893.55 | kg/m3 | 343.15 | Surface... |
| ρl | 893.40 | kg/m3 | 343.15 | Thermop... |
| ρl | 889.70 | kg/m3 | 348.15 | Thermop... |
| ρl | 888.41 | kg/m3 | 348.15 | Surface... |
| ρl | 884.60 | kg/m3 | 353.15 | Thermop... |
| ρl | 883.24 | kg/m3 | 353.15 | Surface... |
| ρl | 878.04 | kg/m3 | 358.15 | Surface... |
| ρl | 879.40 | kg/m3 | 358.15 | Thermop... |
| ρl | 872.81 | kg/m3 | 363.15 | Surface... |
| ρl | 874.20 | kg/m3 | 363.15 | Thermop... |
| ρl | 869.00 | kg/m3 | 368.15 | Thermop... |
| ρl | 863.80 | kg/m3 | 373.15 | Thermop... |
| ΔfusS | 85.10 | J/mol×K | 209.10 | NIST |
| γ | [0.02; 0.03] | N/m | [298.15; 318.15] |
|
| γ | 0.02 | N/m | 298.15 | Volumet... |
| γ | 0.03 | N/m | 308.15 | Volumet... |
| γ | 0.02 | N/m | 318.15 | Volumet... |
| λ | [0.11; 0.15] | W/m×K | [302.75; 392.16] |
|
| λ | 0.15 | W/m×K | 302.75 | Thermal... |
| λ | 0.13 | W/m×K | 332.54 | Thermal... |
| λ | 0.12 | W/m×K | 362.39 | Thermal... |
| λ | 0.11 | W/m×K | 392.16 | Thermal... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.69 | 100.00 | 953.48 |
| 283.69 | 1000.00 | 954.15 |
| 283.69 | 5000.00 | 956.94 |
| 283.68 | 10000.00 | 960.29 |
| 283.68 | 20000.00 | 966.68 |
| 283.68 | 30000.00 | 972.8 |
| 283.67 | 40000.00 | 978.49 |
| 283.67 | 60000.00 | 989.12 |
| 283.67 | 80000.00 | 998.75 |
| 283.67 | 100000.00 | 1007.71 |
| 303.47 | 100.00 | 933.69 |
| 303.47 | 1000.00 | 934.43 |
| 303.48 | 5000.00 | 937.55 |
| 303.48 | 10000.00 | 941.31 |
| 322.62 | 30000.00 | 938.31 |
| 322.62 | 40000.00 | 945.16 |
| 322.62 | 60000.00 | 957.74 |
| 322.62 | 80000.00 | 968.98 |
| 322.62 | 100000.00 | 979.2 |
| 342.49 | 100.00 | 894.03 |
| 342.49 | 1000.00 | 894.98 |
| 342.49 | 5000.00 | 898.96 |
| 342.50 | 10000.00 | 903.66 |
| 342.50 | 20000.00 | 912.57 |
| 342.51 | 30000.00 | 920.68 |
| 342.51 | 40000.00 | 928.18 |
| 342.51 | 60000.00 | 941.77 |
| 342.51 | 80000.00 | 953.82 |
| 303.49 | 20000.00 | 948.42 |
| 303.49 | 30000.00 | 955.17 |
| 303.49 | 40000.00 | 961.41 |
| 303.49 | 60000.00 | 973.02 |
| 303.50 | 80000.00 | 983.33 |
| 303.50 | 100000.00 | 992.97 |
| 322.62 | 100.00 | 914.41 |
| 322.62 | 1000.00 | 915.3 |
| 322.62 | 5000.00 | 918.77 |
| 322.62 | 10000.00 | 923.02 |
| 322.62 | 20000.00 | 930.99 |
| 342.52 | 100000.00 | 964.68 |
| 362.51 | 100.00 | 873.45 |
| 362.51 | 1000.00 | 874.46 |
| 362.51 | 5000.00 | 879.02 |
| 362.52 | 10000.00 | 884.41 |
| 362.52 | 20000.00 | 894.33 |
| 362.52 | 30000.00 | 903.29 |
| 362.52 | 40000.00 | 911.53 |
| 362.53 | 60000.00 | 926.3 |
| 362.53 | 80000.00 | 939.26 |
| 362.53 | 100000.00 | 950.89 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 943.5 |
| 293.15 | 5000.00 | 947.3 |
| 293.15 | 10000.00 | 950.9 |
| 293.15 | 15000.00 | 954.4 |
| 293.15 | 20000.00 | 957.7 |
| 293.15 | 25000.00 | 960.9 |
| 293.15 | 30000.00 | 964.0 |
| 293.15 | 35000.00 | 967.0 |
| 293.15 | 40000.00 | 969.8 |
| 293.15 | 45000.00 | 972.8 |
| 293.15 | 50000.00 | 975.4 |
| 293.15 | 55000.00 | 978.2 |
| 293.15 | 60000.00 | 980.9 |
| 303.15 | 100.00 | 933.7 |
| 303.15 | 5000.00 | 937.6 |
| 303.15 | 10000.00 | 941.1 |
| 303.15 | 15000.00 | 945.0 |
| 303.15 | 20000.00 | 948.4 |
| 303.15 | 25000.00 | 951.8 |
| 303.15 | 30000.00 | 955.2 |
| 303.15 | 35000.00 | 958.2 |
| 303.15 | 40000.00 | 961.1 |
| 303.15 | 45000.00 | 964.0 |
| 303.15 | 50000.00 | 967.3 |
| 303.15 | 55000.00 | 970.1 |
| 303.15 | 60000.00 | 973.2 |
| 313.15 | 100.00 | 923.7 |
| 313.15 | 5000.00 | 927.9 |
| 313.15 | 10000.00 | 931.8 |
| 313.15 | 15000.00 | 935.7 |
| 313.15 | 20000.00 | 939.4 |
| 313.15 | 25000.00 | 942.6 |
| 313.15 | 30000.00 | 946.5 |
| 313.15 | 35000.00 | 949.7 |
| 313.15 | 40000.00 | 952.8 |
| 313.15 | 45000.00 | 956.1 |
| 313.15 | 50000.00 | 958.8 |
| 313.15 | 55000.00 | 961.9 |
| 313.15 | 60000.00 | 964.9 |
| 323.15 | 100.00 | 913.7 |
| 323.15 | 5000.00 | 918.2 |
| 323.15 | 10000.00 | 922.7 |
| 323.15 | 15000.00 | 926.4 |
| 323.15 | 20000.00 | 930.5 |
| 323.15 | 25000.00 | 934.2 |
| 323.15 | 30000.00 | 937.6 |
| 323.15 | 35000.00 | 941.0 |
| 323.15 | 40000.00 | 944.4 |
| 323.15 | 45000.00 | 947.6 |
| 323.15 | 50000.00 | 951.0 |
| 323.15 | 55000.00 | 953.9 |
| 323.15 | 60000.00 | 956.7 |
| 333.15 | 100.00 | 903.6 |
| 333.15 | 5000.00 | 908.3 |
| 333.15 | 10000.00 | 912.8 |
| 333.15 | 15000.00 | 917.3 |
| 333.15 | 20000.00 | 921.0 |
| 333.15 | 25000.00 | 925.3 |
| 333.15 | 30000.00 | 928.9 |
| 333.15 | 35000.00 | 932.6 |
| 333.15 | 40000.00 | 936.4 |
| 333.15 | 45000.00 | 939.8 |
| 333.15 | 50000.00 | 942.9 |
| 333.15 | 55000.00 | 946.0 |
| 333.15 | 60000.00 | 949.1 |
| 343.15 | 100.00 | 893.6 |
| 343.15 | 5000.00 | 898.5 |
| 343.15 | 10000.00 | 903.2 |
| 343.15 | 15000.00 | 907.8 |
| 343.15 | 20000.00 | 912.3 |
| 343.15 | 25000.00 | 916.2 |
| 343.15 | 30000.00 | 920.5 |
| 343.15 | 35000.00 | 924.2 |
| 343.15 | 40000.00 | 928.0 |
| 343.15 | 45000.00 | 931.4 |
| 343.15 | 50000.00 | 934.8 |
| 343.15 | 55000.00 | 938.2 |
| 343.15 | 60000.00 | 941.4 |
| 353.15 | 100.00 | 883.3 |
| 353.15 | 5000.00 | 888.7 |
| 353.15 | 10000.00 | 893.9 |
| 353.15 | 15000.00 | 898.7 |
| 353.15 | 20000.00 | 903.2 |
| 353.15 | 25000.00 | 907.6 |
| 353.15 | 30000.00 | 911.6 |
| 353.15 | 35000.00 | 915.5 |
| 353.15 | 40000.00 | 919.5 |
| 353.15 | 45000.00 | 923.1 |
| 353.15 | 50000.00 | 927.0 |
| 353.15 | 55000.00 | 930.4 |
| 353.15 | 60000.00 | 933.6 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 100.00 | 1298.9 |
| 293.15 | 10000.00 | 1344.9 |
| 293.15 | 20000.00 | 1386.5 |
| 293.15 | 30000.00 | 1426.6 |
| 293.15 | 40000.00 | 1463.9 |
| 293.15 | 50000.00 | 1499.2 |
| 293.15 | 60000.00 | 1532.5 |
| 293.15 | 70000.00 | 1565.1 |
| 293.15 | 80000.00 | 1595.5 |
| 293.15 | 90000.00 | 1624.9 |
| 293.15 | 100000.00 | 1653.4 |
| 303.15 | 100.00 | 1259.3 |
| 303.15 | 10000.00 | 1306.7 |
| 303.15 | 20000.00 | 1350.6 |
| 303.15 | 30000.00 | 1392.0 |
| 303.15 | 40000.00 | 1430.4 |
| 303.15 | 50000.00 | 1466.9 |
| 303.15 | 60000.00 | 1501.5 |
| 303.15 | 70000.00 | 1534.3 |
| 303.15 | 80000.00 | 1565.8 |
| 303.15 | 90000.00 | 1595.9 |
| 303.15 | 100000.00 | 1625.1 |
| 313.15 | 100.00 | 1219.9 |
| 313.15 | 10000.00 | 1269.5 |
| 313.15 | 20000.00 | 1315.4 |
| 313.15 | 30000.00 | 1357.6 |
| 313.15 | 40000.00 | 1397.8 |
| 313.15 | 50000.00 | 1435.3 |
| 313.15 | 60000.00 | 1470.5 |
| 313.15 | 70000.00 | 1504.4 |
| 313.15 | 80000.00 | 1536.7 |
| 313.15 | 90000.00 | 1567.6 |
| 313.15 | 100000.00 | 1597.0 |
| 323.15 | 100.00 | 1180.9 |
| 323.15 | 10000.00 | 1232.5 |
| 323.15 | 20000.00 | 1280.2 |
| 323.15 | 30000.00 | 1324.4 |
| 323.15 | 40000.00 | 1365.5 |
| 323.15 | 50000.00 | 1404.0 |
| 323.15 | 60000.00 | 1440.6 |
| 323.15 | 70000.00 | 1475.2 |
| 323.15 | 80000.00 | 1508.2 |
| 323.15 | 90000.00 | 1539.8 |
| 323.15 | 100000.00 | 1569.9 |
| 333.15 | 100.00 | 1142.4 |
| 333.15 | 10000.00 | 1196.4 |
| 333.15 | 20000.00 | 1246.0 |
| 333.15 | 30000.00 | 1291.4 |
| 333.15 | 40000.00 | 1333.7 |
| 333.15 | 50000.00 | 1373.6 |
| 333.15 | 60000.00 | 1410.9 |
| 333.15 | 70000.00 | 1446.2 |
| 333.15 | 80000.00 | 1480.1 |
| 333.15 | 90000.00 | 1512.3 |
| 333.15 | 100000.00 | 1543.1 |
| 343.15 | 100.00 | 1104.2 |
| 343.15 | 10000.00 | 1160.8 |
| 343.15 | 20000.00 | 1212.0 |
| 343.15 | 30000.00 | 1259.5 |
| 343.15 | 40000.00 | 1303.1 |
| 343.15 | 50000.00 | 1343.9 |
| 343.15 | 60000.00 | 1382.1 |
| 343.15 | 70000.00 | 1418.6 |
| 343.15 | 80000.00 | 1452.9 |
| 343.15 | 90000.00 | 1485.9 |
| 343.15 | 100000.00 | 1517.4 |
| 353.15 | 100.00 | 1066.6 |
| 353.15 | 10000.00 | 1125.7 |
| 353.15 | 20000.00 | 1179.3 |
| 353.15 | 30000.00 | 1228.1 |
| 353.15 | 40000.00 | 1273.4 |
| 353.15 | 50000.00 | 1314.9 |
| 353.15 | 60000.00 | 1354.4 |
| 353.15 | 70000.00 | 1391.3 |
| 353.15 | 80000.00 | 1426.7 |
| 353.15 | 90000.00 | 1460.4 |
| 353.15 | 100000.00 | 1492.3 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [322.72; 461.92] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.56921e+01 | |||
| Coefficient B | -4.43052e+03 | |||
| Coefficient C | -3.51090e+01 | |||
| Temperature range, min. | 322.72 | |||
| Temperature range, max. | 461.92 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 322.72 | Calculated Property |
| Pvap | 2.93 | kPa | 338.19 | Calculated Property |
| Pvap | 5.95 | kPa | 353.65 | Calculated Property |
| Pvap | 11.33 | kPa | 369.12 | Calculated Property |
| Pvap | 20.38 | kPa | 384.59 | Calculated Property |
| Pvap | 34.88 | kPa | 400.05 | Calculated Property |
| Pvap | 57.14 | kPa | 415.52 | Calculated Property |
| Pvap | 90.06 | kPa | 430.99 | Calculated Property |
| Pvap | 137.18 | kPa | 446.45 | Calculated Property |
| Pvap | 202.67 | kPa | 461.92 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, 1,1'-oxybis[2-methoxy-.
Mixtures
- Carbon dioxide + Ethane, 1,1'-oxybis[2-methoxy-
- Ethane, 1,1'-oxybis[2-methoxy- + 1-Butanol
- Ethanol + Ethane, 1,1'-oxybis[2-methoxy-
- Ethane, 1,1'-oxybis[2-methoxy- + Cyclohexane + «beta» Carotene
- n-Hexane + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
- Toluene + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
- 1-Hexene + Ethane, 1,1'-oxybis[2-methoxy- + «beta» Carotene
- Ethane, 1,1'-oxybis[2-methoxy- + Water
- Ethane, 1,1'-oxybis[2-methoxy- + Ethane, 1,2-dichloro-
- Ethane, 1,1'-oxybis[2-methoxy- + Norflurane
- Difluoromethane + Ethane, 1,1'-oxybis[2-methoxy-
- Ethane, 1,1'-oxybis[2-methoxy- + Ethane, 1,1-difluoro-
- Ethane, 1,1'-oxybis[2-methoxy- + Propane, 1,1,1,3,3-pentafluoro
- Methane + Ethane, 1,1'-oxybis[2-methoxy-
- Ethane + Ethane, 1,1'-oxybis[2-methoxy-
- Ethane, 1,1'-oxybis[2-methoxy- + Propane, 1,1,1,3,3,3-hexafluoro-
Sources
- Crippen Method
- Temperature and Pressure Dependences of Thermophysical Properties of Some Ethylene Glycol Dimethyl Ethers from Ultrasonic Measurements
- Density, viscosity and solubility of carbon dioxide in glymes
- Vapor-liquid equilibria of difluoromethane + N,N-dimethylacetamide, difluoromethane + dimethylether diethylene glycol and 1,1-difluoroethane + dimethylether diethylene glycol systems
- Vapor-liquid equilibrium measurement of1,1,1,3,3-pentafluoropropane + N,N-dimethylformamide/diethyleneglycol dimethyl ether/N-methyl-2-pyrrolidone working fluids forabsorption power cycle
- Surface tension of four oxygenated fuels: experiment and correlation
- Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
- Non-ideal behaviour of a room temperature ionic liquid in an alkoxyethanol or poly ethers at T = (298.15 to 318.15) K
- Thermophysical properties of glycols and glymes
- Isothermal Vapor Liquid Equilibrium of HFC-161 + DMETrEG within the Temperature Range of 293.15 353.15 K and Comparison for HFC-161 Combined with Different Absorbents
- Compressed Liquid Densities of Binary Mixtures of 1-Butanol and Diethylene Glycol Dimethyl Ether from (283 to 363) K at Pressures up to 100 MPa
- Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
- Volumetric Properties of Monoethylene Glycol Dimethyl Ether and Diethylene Glycol Dimethyl Ether up to 60 MPa
- Solubility Study of Methane and Ethane In Promising Physical Solvents for Natural Gas Sweetening Operations
- Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
- Volumetric and Surface Properties of Aqueous Mixtures of Polyethers at T = (298.15, 308.15, and 318.15) K
- Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
- Excess Properties and Spectral Investigation for the Binary System Diethylene Glycol Dimethyl Ether + Water at T = (293.15, 298.15, 303.15, 308.15 and 313.15) K
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of 1,1,1,3,3-Pentafluoropropane + N,N-Dimethylacetamide and 1,1,1,3,3,3-Hexafluoropropane + N,N-Dimethylacetamide/Diethylene Glycol Dimethyl Ether Systems
- Thermal Conductivity Measurement of Polyglycol Alkyl Ethers at Temperatures from (303.15 to 393.15) K
- p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
- Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
- Joback Method
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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