- InChI
- InChI=1S/C6H12O/c1-3-5-6-7-4-2/h4H,2-3,5-6H2,1H3
- InChI Key
- UZKWTJUDCOPSNM-UHFFFAOYSA-N
- Formula
- C6H12O
- SMILES
- C=COCCCC
- Molecular Weight1
- 100.16
- CAS
- 111-34-2
- Other Names
-
- 1-(ETHYNYLOXY)BUTANE
- 1-(Ethenyloxy)butane
- 1-(Vinyloxy)-butane
- 1-(vinyloxy)butane
- 1-Butoxyethylene
- 1-vinyloxybutane
- BUTOXYETHENE
- BVE
- Butoxyethylene
- Butyl vinyl ether
- Ethenyl n-butyl ether
- Ether, butyl vinyl
- NSC 8264
- VINYL N-BUTYL ETHER
- Vinyl butyl ether
- n-Butyl vinyl ether
- n-C4H9OCH=CH2
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- 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.
- 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 |
|---|---|---|---|
| ΔcH°liquid | [-3860.20; -3857.00] | kJ/mol |
|
| ΔcH°liquid | -3860.20 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -3857.00 ± 0.80 | kJ/mol | NIST |
| ΔfG° | -17.52 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-182.40; -179.20] | kJ/mol |
|
| ΔfH°gas | -179.20 ± 1.20 | kJ/mol | NIST |
| ΔfH°gas | -182.40 | kJ/mol | NIST |
| ΔfH°liquid | [-219.00; -215.80] | kJ/mol |
|
| ΔfH°liquid | -215.80 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -219.00 ± 0.80 | kJ/mol | NIST |
| ΔfusH° | 11.20 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 30.69 | kJ/mol | Joback Calculated Property |
| log10WS | -1.77 | Crippen Calculated Property | |
| logPoct/wat | 1.947 | Crippen Calculated Property | |
| McVol | 96.970 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | 3200.00 ± 250.00 | kPa | NIST |
| ρc | 261.11 ± 12.02 | kg/m3 | NIST |
| Inp | [671.00; 695.00] |
|
|
| Inp | 695.00 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 679.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 695.00 | NIST | |
| I | 858.00 | NIST | |
| Tboil | [366.00; 367.10] | K |
|
| Tboil | 367.00 | K | NIST |
| Tboil | 366.00 | K | NIST |
| Tboil | 367.10 | K | NIST |
| Tc | 540.50 ± 2.00 | K | NIST |
| Tfus | 177.85 | K | Joback Calculated Property |
| Vc | 0.370 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [168.37; 221.32] | J/mol×K | [355.78; 523.68] |
|
| Cp,gas | 168.37 | J/mol×K | 355.78 | Joback Calculated Property |
| Cp,gas | 177.92 | J/mol×K | 383.76 | Joback Calculated Property |
| Cp,gas | 187.18 | J/mol×K | 411.75 | Joback Calculated Property |
| Cp,gas | 196.15 | J/mol×K | 439.73 | Joback Calculated Property |
| Cp,gas | 204.82 | J/mol×K | 467.71 | Joback Calculated Property |
| Cp,gas | 213.21 | J/mol×K | 495.69 | Joback Calculated Property |
| Cp,gas | 221.32 | J/mol×K | 523.68 | Joback Calculated Property |
| Cp,liquid | 231.80 | J/mol×K | 298.15 | NIST |
| η | [0.0002123; 0.0029205] | Pa×s | [177.85; 355.78] |
|
| η | 0.0029205 | Pa×s | 177.85 | Joback Calculated Property |
| η | 0.0013807 | Pa×s | 207.51 | Joback Calculated Property |
| η | 0.0007872 | Pa×s | 237.16 | Joback Calculated Property |
| η | 0.0005086 | Pa×s | 266.81 | Joback Calculated Property |
| η | 0.0003585 | Pa×s | 296.47 | Joback Calculated Property |
| η | 0.0002694 | Pa×s | 326.12 | Joback Calculated Property |
| η | 0.0002123 | Pa×s | 355.78 | Joback Calculated Property |
| ΔvapH | [29.60; 36.10] | kJ/mol | [318.50; 367.10] |
|
| ΔvapH | 36.10 | kJ/mol | 318.50 | NIST |
| ΔvapH | 35.20 ± 0.20 | kJ/mol | 357.00 | NIST |
| ΔvapH | 32.50 ± 0.20 | kJ/mol | 357.00 | NIST |
| ΔvapH | 29.60 ± 0.20 | kJ/mol | 357.00 | NIST |
| ΔvapH | 31.58 | kJ/mol | 367.10 | NIST |
| ρl | [758.80; 780.20] | kg/m3 | [298.15; 313.15] |
|
| ρl | 780.20 | kg/m3 | 298.15 | Densiti... |
| ρl | 769.00 | kg/m3 | 303.15 | Density... |
| ρl | 774.10 | kg/m3 | 303.15 | Densiti... |
| ρl | 763.90 | kg/m3 | 308.15 | Density... |
| ρl | 768.20 | kg/m3 | 308.15 | Densiti... |
| ρl | 758.80 | kg/m3 | 313.15 | Density... |
| ρl | 763.30 | kg/m3 | 313.15 | Densiti... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [274.58; 389.11] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54615e+01 | |||
| Coefficient B | -3.51136e+03 | |||
| Coefficient C | -4.31680e+01 | |||
| Temperature range, min. | 274.58 | |||
| Temperature range, max. | 389.11 | |||
| Pvap | 1.33 | kPa | 274.58 | Calculated Property |
| Pvap | 2.94 | kPa | 287.31 | Calculated Property |
| Pvap | 6.00 | kPa | 300.03 | Calculated Property |
| Pvap | 11.43 | kPa | 312.76 | Calculated Property |
| Pvap | 20.57 | kPa | 325.48 | Calculated Property |
| Pvap | 35.17 | kPa | 338.21 | Calculated Property |
| Pvap | 57.53 | kPa | 350.93 | Calculated Property |
| Pvap | 90.49 | kPa | 363.66 | Calculated Property |
| Pvap | 137.51 | kPa | 376.38 | Calculated Property |
| Pvap | 202.62 | kPa | 389.11 | Calculated Property |
| Pvap | [1.31e-04; 3086.33] | kPa | [181.15; 536.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.18610e+01 | |||
| Coefficient B | -7.10617e+03 | |||
| Coefficient C | -9.96430e+00 | |||
| Coefficient D | 7.13053e-06 | |||
| Temperature range, min. | 181.15 | |||
| Temperature range, max. | 536.00 | |||
| Pvap | 1.31e-04 | kPa | 181.15 | Calculated Property |
| Pvap | 0.02 | kPa | 220.58 | Calculated Property |
| Pvap | 0.67 | kPa | 260.01 | Calculated Property |
| Pvap | 7.05 | kPa | 299.43 | Calculated Property |
| Pvap | 38.90 | kPa | 338.86 | Calculated Property |
| Pvap | 141.40 | kPa | 378.29 | Calculated Property |
| Pvap | 387.84 | kPa | 417.72 | Calculated Property |
| Pvap | 875.73 | kPa | 457.14 | Calculated Property |
| Pvap | 1725.20 | kPa | 496.57 | Calculated Property |
| Pvap | 3086.33 | kPa | 536.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Butane, 1-(ethenyloxy)-.
Mixtures
- Acetic acid ethenyl ester + Butane, 1-(ethenyloxy)-
- Butane, 1-(ethenyloxy)- + Acetic acid, hexyl ester
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
- Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
- Joback Method
- KDB
- 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.