![Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-](/cid/51-649-5/Butane-1-1-oxybis-2-1-ethanediyloxy-bis.png "Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-")
- InChI
- InChI=1S/C12H26O3/c1-3-5-7-13-9-11-15-12-10-14-8-6-4-2/h3-12H2,1-2H3
- InChI Key
- KZVBBTZJMSWGTK-UHFFFAOYSA-N
- Formula
- C12H26O3
- SMILES
- CCCCOCCOCCOCCCC
- Molecular Weight1
- 218.33
- CAS
- 112-73-2
- Other Names
-
- 2,2'-Dibutoxyethyl ether
- 2-(2-Butoxyethoxy)-1-butoxyethane
- 2-Butoxyethyl ether
- 5,8,11-Trioxapentadecane
- Bis(2-butoxyethyl) ether
- Butex
- Butyl diglyme
- Dibutyl carbitol
- Dibutylether diethylenglykolu
- Diethylene glycol di-n-butyl ether
- Diethylene glycol dibutyl ether
- Ether, bis(2-butoxyethyl)
- Ether, bis(butoxyethyl)
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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).
- ρl : Liquid Density (kg/m3).
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -264.84 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -687.67 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 30.40 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 73.80 ± 1.70 | kJ/mol | NIST |
| log10WS | -2.11 | Crippen Calculated Property | |
| logPoct/wat | 2.636 | Crippen Calculated Property | |
| McVol | 197.550 | ml/mol | McGowan Calculated Property |
| Pc | 1706.12 | kPa | Joback Calculated Property |
| I | 1727.00 | NIST | |
| Tboil | [529.15; 529.20] | K |
|
| Tboil | 529.20 | K | NIST |
| Tboil | 529.15 | K | NIST |
| Tboil | 529.15 | K | NIST |
| Tc | 702.31 | K | Joback Calculated Property |
| Tfus | [212.95; 212.95] | K |
|
| Tfus | 212.95 | K | NIST |
| Tfus | 212.95 | K | NIST |
| Vc | 0.761 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [493.03; 581.29] | J/mol×K | [541.22; 702.31] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 500 520 540 560 580 550 600 650 700 | ||||
| Cp,gas | 493.03 | J/mol×K | 541.22 | Joback Calculated Property |
| Cp,gas | 509.02 | J/mol×K | 568.07 | Joback Calculated Property |
| Cp,gas | 524.51 | J/mol×K | 594.92 | Joback Calculated Property |
| Cp,gas | 539.48 | J/mol×K | 621.77 | Joback Calculated Property |
| Cp,gas | 553.94 | J/mol×K | 648.62 | Joback Calculated Property |
| Cp,gas | 567.88 | J/mol×K | 675.46 | Joback Calculated Property |
| Cp,gas | 581.29 | J/mol×K | 702.31 | Joback Calculated Property |
| Cp,liquid | [456.53; 517.89] | J/mol×K | [312.57; 421.48] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 460 470 480 490 500 510 520 350 400 | ||||
| Cp,liquid | 456.53 | J/mol×K | 312.57 | Liquid ... |
| Cp,liquid | 460.90 | J/mol×K | 322.47 | Liquid ... |
| Cp,liquid | 465.49 | J/mol×K | 332.37 | Liquid ... |
| Cp,liquid | 470.51 | J/mol×K | 342.27 | Liquid ... |
| Cp,liquid | 475.75 | J/mol×K | 352.18 | Liquid ... |
| Cp,liquid | 480.33 | J/mol×K | 362.08 | Liquid ... |
| Cp,liquid | 486.88 | J/mol×K | 371.98 | Liquid ... |
| Cp,liquid | 493.65 | J/mol×K | 381.88 | Liquid ... |
| Cp,liquid | 500.42 | J/mol×K | 391.78 | Liquid ... |
| Cp,liquid | 505.44 | J/mol×K | 401.68 | Liquid ... |
| Cp,liquid | 512.21 | J/mol×K | 411.58 | Liquid ... |
| Cp,liquid | 517.89 | J/mol×K | 421.48 | Liquid ... |
| η | [0.0001158; 0.0020127] | Pa×s | [291.69; 541.22] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 300 400 500 | ||||
| η | 0.0020127 | Pa×s | 291.69 | Joback Calculated Property |
| η | 0.0009292 | Pa×s | 333.28 | Joback Calculated Property |
| η | 0.0005093 | Pa×s | 374.87 | Joback Calculated Property |
| η | 0.0003147 | Pa×s | 416.46 | Joback Calculated Property |
| η | 0.0002123 | Pa×s | 458.04 | Joback Calculated Property |
| η | 0.0001529 | Pa×s | 499.63 | Joback Calculated Property |
| η | 0.0001158 | Pa×s | 541.22 | Joback Calculated Property |
| ΔvapH | 56.60 | kJ/mol | 410.50 | NIST |
| Pvap | [2.50; 25.58] | kPa | [403.15; 473.15] |
|
|
T(K) Vapor pressure (kPa) 5 10 15 20 25 420 440 460 | ||||
| Pvap | 2.50 | kPa | 403.15 | Vapor P... |
| Pvap | 3.61 | kPa | 413.15 | Vapor P... |
| Pvap | 5.26 | kPa | 423.15 | Vapor P... |
| Pvap | 7.39 | kPa | 433.15 | Vapor P... |
| Pvap | 10.43 | kPa | 443.15 | Vapor P... |
| Pvap | 14.23 | kPa | 453.15 | Vapor P... |
| Pvap | 16.61 | kPa | 458.15 | Vapor P... |
| Pvap | 19.19 | kPa | 463.15 | Vapor P... |
| Pvap | 22.18 | kPa | 468.15 | Vapor P... |
| Pvap | 25.58 | kPa | 473.15 | Vapor P... |
| ρl | 878.55 | kg/m3 | 298.15 | Speeds ... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 891.3 |
| 283.15 | 1000.00 | 891.8 |
| 283.15 | 3000.00 | 893.2 |
| 283.15 | 5000.00 | 894.3 |
| 283.15 | 10000.00 | 897.7 |
| 283.15 | 15000.00 | 900.9 |
| 283.15 | 20000.00 | 904.3 |
| 283.15 | 25000.00 | 906.9 |
| 283.15 | 30000.00 | 909.9 |
| 283.15 | 35000.00 | 912.8 |
| 283.15 | 40000.00 | 915.3 |
| 283.15 | 50000.00 | 920.5 |
| 283.15 | 60000.00 | 925.4 |
| 293.15 | 100.00 | 882.9 |
| 293.15 | 1000.00 | 883.1 |
| 293.15 | 3000.00 | 884.8 |
| 293.15 | 5000.00 | 885.9 |
| 293.15 | 10000.00 | 889.6 |
| 293.15 | 15000.00 | 892.9 |
| 293.15 | 20000.00 | 896.1 |
| 293.15 | 25000.00 | 899.3 |
| 293.15 | 30000.00 | 902.3 |
| 293.15 | 35000.00 | 905.1 |
| 293.15 | 40000.00 | 907.9 |
| 293.15 | 50000.00 | 913.6 |
| 293.15 | 60000.00 | 918.2 |
| 303.15 | 100.00 | 874.5 |
| 303.15 | 1000.00 | 875.1 |
| 303.15 | 3000.00 | 876.6 |
| 303.15 | 5000.00 | 878.2 |
| 303.15 | 10000.00 | 881.8 |
| 303.15 | 15000.00 | 885.2 |
| 303.15 | 20000.00 | 888.42 |
| 303.15 | 25000.00 | 891.8 |
| 303.15 | 30000.00 | 894.9 |
| 303.15 | 35000.00 | 897.9 |
| 303.15 | 40000.00 | 900.8 |
| 303.15 | 50000.00 | 906.4 |
| 303.15 | 60000.00 | 911.8 |
| 313.15 | 100.00 | 866.1 |
| 313.15 | 1000.00 | 866.41 |
| 313.15 | 3000.00 | 868.1 |
| 313.15 | 5000.00 | 869.8 |
| 313.15 | 10000.00 | 873.5 |
| 313.15 | 15000.00 | 877.2 |
| 313.15 | 20000.00 | 880.7 |
| 313.15 | 25000.00 | 884.1 |
| 313.15 | 30000.00 | 887.1 |
| 313.15 | 35000.00 | 890.5 |
| 313.15 | 40000.00 | 893.3 |
| 313.15 | 50000.00 | 899.4 |
| 313.15 | 60000.00 | 904.9 |
| 323.15 | 100.00 | 857.2 |
| 323.15 | 1000.00 | 858.2 |
| 323.15 | 3000.00 | 859.8 |
| 323.15 | 5000.00 | 861.5 |
| 323.15 | 10000.00 | 865.4 |
| 323.15 | 15000.00 | 869.2 |
| 323.15 | 20000.00 | 873.1 |
| 323.15 | 25000.00 | 876.5 |
| 323.15 | 30000.00 | 879.8 |
| 323.15 | 35000.00 | 883.1 |
| 323.15 | 40000.00 | 886.3 |
| 323.15 | 50000.00 | 892.4 |
| 323.15 | 60000.00 | 898.8 |
| 333.15 | 100.00 | 849.1 |
| 333.15 | 1000.00 | 850.0 |
| 333.15 | 3000.00 | 851.6 |
| 333.15 | 5000.00 | 853.3 |
| 333.15 | 10000.00 | 857.5 |
| 333.15 | 15000.00 | 861.4 |
| 333.15 | 20000.00 | 865.4 |
| 333.15 | 25000.00 | 869.0 |
| 333.15 | 30000.00 | 872.6 |
| 333.15 | 35000.00 | 875.9 |
| 333.15 | 40000.00 | 879.5 |
| 333.15 | 50000.00 | 885.5 |
| 333.15 | 60000.00 | 891.6 |
| 343.15 | 100.00 | 840.4 |
| 343.15 | 1000.00 | 841.7 |
| 343.15 | 3000.00 | 843.5 |
| 343.15 | 5000.00 | 845.5 |
| 343.15 | 10000.00 | 849.8 |
| 343.15 | 15000.00 | 853.7 |
| 343.15 | 20000.00 | 857.9 |
| 343.15 | 25000.00 | 861.6 |
| 343.15 | 30000.00 | 865.3 |
| 343.15 | 35000.00 | 868.9 |
| 343.15 | 40000.00 | 872.3 |
| 343.15 | 50000.00 | 878.9 |
| 343.15 | 60000.00 | 884.7 |
| 353.15 | 100.00 | 832.4 |
| 353.15 | 1000.00 | 833.0 |
| 353.15 | 3000.00 | 835.1 |
| 353.15 | 5000.00 | 836.7 |
| 353.15 | 10000.00 | 841.4 |
| 353.15 | 15000.00 | 846.0 |
| 353.15 | 20000.00 | 850.3 |
| 353.15 | 25000.00 | 854.0 |
| 353.15 | 30000.00 | 857.9 |
| 353.15 | 35000.00 | 861.6 |
| 353.15 | 40000.00 | 865.1 |
| 353.15 | 50000.00 | 871.5 |
| 353.15 | 60000.00 | 878.2 |
| 363.15 | 100.00 | 823.4 |
| 363.15 | 1000.00 | 824.8 |
| 363.15 | 3000.00 | 827.1 |
| 363.15 | 5000.00 | 828.7 |
| 363.15 | 10000.00 | 833.5 |
| 363.15 | 15000.00 | 838.4 |
| 363.15 | 20000.00 | 842.8 |
| 363.15 | 25000.00 | 846.8 |
| 363.15 | 30000.00 | 850.9 |
| 363.15 | 35000.00 | 854.9 |
| 363.15 | 40000.00 | 858.5 |
| 363.15 | 50000.00 | 865.6 |
| 363.15 | 60000.00 | 872.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [398.87; 559.05] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.69660e+01 | |||
| Coefficient B | -6.19763e+03 | |||
| Coefficient C | -2.72730e+01 | |||
| Temperature range, min. | 398.87 | |||
| Temperature range, max. | 559.05 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 550 | ||||
| Pvap | 1.33 | kPa | 398.87 | Calculated Property |
| Pvap | 2.86 | kPa | 416.67 | Calculated Property |
| Pvap | 5.73 | kPa | 434.47 | Calculated Property |
| Pvap | 10.84 | kPa | 452.26 | Calculated Property |
| Pvap | 19.48 | kPa | 470.06 | Calculated Property |
| Pvap | 33.45 | kPa | 487.86 | Calculated Property |
| Pvap | 55.18 | kPa | 505.66 | Calculated Property |
| Pvap | 87.83 | kPa | 523.45 | Calculated Property |
| Pvap | 135.35 | kPa | 541.25 | Calculated Property |
| Pvap | 202.64 | kPa | 559.05 | Calculated Property |
Similar Compounds
![Ethanol, 2-[2-(2-butoxyethoxy)ethoxy]-.](data:image/png;base64,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)
![2-[2-[2-(2-Butoxyethoxy)ethoxy]ethoxy]ethyl acetate.](data:image/png;base64,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)
![2-[2-[2-[2-(2-Butoxyethoxy)ethoxy]ethoxy]ethoxy]ethyl acetate.](data:image/png;base64,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)
Find more compounds similar to Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-.
Mixtures
- Propylamine + Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-
- Carbon dioxide + Butane, 1,1'-[oxybis(2,1-ethanediyloxy)]bis-
Sources
- Crippen Method
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities of n-Alkoxyethanols and Polyethers with Propylamine at 298.15K
- Densities of Diethylene Glycol, Monobutyl Ether, Diethylene Glycol Dibutyl Ether, and Ethylene Glycol Monobutyl Ether from (283.15 to 363.15) K at Pressures up to 60 MPa
- Solubility Measurement and Thermodynamic Properties Calculation for Several CO2 + Ether Absorbent Systems
- Liquid Densities, Kinematic Viscosities, and Heat Capacities of Some Alkylene glycol Dialkyl Ethers
- Vapor Pressures of Morpholine, Diethyl Methylmalonate, and Five Glycol Ethers at Temperatures up to 473.15 K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.