- InChI
- InChI=1S/C10H22O/c1-9(2)5-7-11-8-6-10(3)4/h9-10H,5-8H2,1-4H3
- InChI Key
- AQZGPSLYZOOYQP-UHFFFAOYSA-N
- Formula
- C10H22O
- SMILES
- CC(C)CCOCCC(C)C
- Molecular Weight1
- 158.28
- CAS
- 544-01-4
- Other Names
-
- 1-isopentyloxy-3-methylbutane
- 2,8-dimethyl-5-oxanonane
- Butane, 1,1'-oxybis[3-methyl-
- DI-ISOPENTYL ETHER
- Di-3-methylbutyl ether
- Diisopentyl ether
- Isoamyl ether
- Isoamyl oxide
- Isopentyl ether
- NSC 9281
- bis(3-methylbutyl) ether
- bis(3-methylbutyl)ether
- di-(3-methylbutyl) ether
- ether, diisoamyl
- ether, diisopentyl
- Cp,gas : Ideal gas 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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° | -76.56 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -392.51 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.80 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [49.94; 51.40] | kJ/mol |
|
| ΔvapH° | 49.94 | kJ/mol | NIST |
| ΔvapH° | 51.40 | kJ/mol | NIST |
| log10WS | -2.61 | Crippen Calculated Property | |
| logPoct/wat | 3.095 | Crippen Calculated Property | |
| McVol | 157.630 | ml/mol | McGowan Calculated Property |
| Pc | 2106.13 | kPa | Joback Calculated Property |
| Inp | [980.00; 1002.00] |
|
|
| Inp | 1002.00 | NIST | |
| Inp | Outlier 980.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1002.00 | NIST | |
| I | [1063.00; 1067.00] |
|
|
| I | 1063.00 | NIST | |
| I | 1064.00 | NIST | |
| I | 1067.00 | NIST | |
| I | 1064.00 | NIST | |
| Tboil | [444.00; 446.50] | K |
|
| Tboil | 445.70 | K | NIST |
| Tboil | 446.40 ± 0.50 | K | NIST |
| Tboil | 446.50 ± 0.35 | K | NIST |
| Tboil | 444.00 ± 4.00 | K | NIST |
| Tboil | 445.80 ± 0.50 | K | NIST |
| Tc | 619.25 | K | Joback Calculated Property |
| Tfus | 194.69 | K | Joback Calculated Property |
| Vc | 0.602 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [342.48; 427.77] | J/mol×K | [449.74; 619.25] |
|
| Cp,gas | 342.48 | J/mol×K | 449.74 | Joback Calculated Property |
| Cp,gas | 358.04 | J/mol×K | 477.99 | Joback Calculated Property |
| Cp,gas | 373.04 | J/mol×K | 506.24 | Joback Calculated Property |
| Cp,gas | 387.51 | J/mol×K | 534.50 | Joback Calculated Property |
| Cp,gas | 401.45 | J/mol×K | 562.75 | Joback Calculated Property |
| Cp,gas | 414.87 | J/mol×K | 591.00 | Joback Calculated Property |
| Cp,gas | 427.77 | J/mol×K | 619.25 | Joback Calculated Property |
| η | [0.0001845; 0.0125876] | Pa×s | [194.69; 449.74] |
|
| η | 0.0125876 | Pa×s | 194.69 | Joback Calculated Property |
| η | 0.0033142 | Pa×s | 237.20 | Joback Calculated Property |
| η | 0.0013091 | Pa×s | 279.71 | Joback Calculated Property |
| η | 0.0006607 | Pa×s | 322.22 | Joback Calculated Property |
| η | 0.0003911 | Pa×s | 364.72 | Joback Calculated Property |
| η | 0.0002583 | Pa×s | 407.23 | Joback Calculated Property |
| η | 0.0001845 | Pa×s | 449.74 | Joback Calculated Property |
| ΔvapH | [41.40; 47.60] | kJ/mol | [369.00; 443.50] |
|
| ΔvapH | 47.60 | kJ/mol | 369.00 | NIST |
| ΔvapH | 41.40 | kJ/mol | 443.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 333.20 | K | 1.30 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 782.76 |
| 288.15 | 100.00 | 778.71 |
| 293.15 | 100.00 | 774.66 |
| 298.15 | 100.00 | 770.6 |
| 303.15 | 100.00 | 766.54 |
| 308.15 | 100.00 | 762.46 |
| 313.15 | 100.00 | 758.37 |
| 318.15 | 100.00 | 754.27 |
| 323.15 | 100.00 | 750.16 |
| 328.15 | 100.00 | 746.03 |
| 333.15 | 100.00 | 741.88 |
| 283.15 | 5000.00 | 786.88 |
| 288.15 | 5000.00 | 782.95 |
| 293.15 | 5000.00 | 779.03 |
| 298.15 | 5000.00 | 775.09 |
| 303.15 | 5000.00 | 771.15 |
| 308.15 | 5000.00 | 767.21 |
| 313.15 | 5000.00 | 763.24 |
| 318.15 | 5000.00 | 759.27 |
| 323.15 | 5000.00 | 755.32 |
| 328.15 | 5000.00 | 751.35 |
| 333.15 | 5000.00 | 747.34 |
| 283.15 | 10000.00 | 790.71 |
| 288.15 | 10000.00 | 786.89 |
| 293.15 | 10000.00 | 783.04 |
| 298.15 | 10000.00 | 779.24 |
| 303.15 | 10000.00 | 775.41 |
| 308.15 | 10000.00 | 771.57 |
| 313.15 | 10000.00 | 767.74 |
| 318.15 | 10000.00 | 763.91 |
| 323.15 | 10000.00 | 760.1 |
| 328.15 | 10000.00 | 756.23 |
| 333.15 | 10000.00 | 752.39 |
| 283.15 | 15000.00 | 794.36 |
| 288.15 | 15000.00 | 790.64 |
| 293.15 | 15000.00 | 786.89 |
| 298.15 | 15000.00 | 783.18 |
| 303.15 | 15000.00 | 779.46 |
| 308.15 | 15000.00 | 775.74 |
| 313.15 | 15000.00 | 772.01 |
| 318.15 | 15000.00 | 768.28 |
| 323.15 | 15000.00 | 764.59 |
| 328.15 | 15000.00 | 760.85 |
| 333.15 | 15000.00 | 757.12 |
| 283.15 | 20000.00 | 797.85 |
| 288.15 | 20000.00 | 794.22 |
| 293.15 | 20000.00 | 790.55 |
| 298.15 | 20000.00 | 786.94 |
| 303.15 | 20000.00 | 783.3 |
| 308.15 | 20000.00 | 779.67 |
| 313.15 | 20000.00 | 776.05 |
| 318.15 | 20000.00 | 772.42 |
| 323.15 | 20000.00 | 768.84 |
| 328.15 | 20000.00 | 765.22 |
| 333.15 | 20000.00 | 761.58 |
| 283.15 | 25000.00 | 801.22 |
| 288.15 | 25000.00 | 797.65 |
| 293.15 | 25000.00 | 794.08 |
| 298.15 | 25000.00 | 790.54 |
| 303.15 | 25000.00 | 786.98 |
| 308.15 | 25000.00 | 783.45 |
| 313.15 | 25000.00 | 779.9 |
| 318.15 | 25000.00 | 776.38 |
| 323.15 | 25000.00 | 772.87 |
| 328.15 | 25000.00 | 769.33 |
| 333.15 | 25000.00 | 765.79 |
| 283.15 | 30000.00 | 804.45 |
| 288.15 | 30000.00 | 800.95 |
| 293.15 | 30000.00 | 797.46 |
| 298.15 | 30000.00 | 793.99 |
| 303.15 | 30000.00 | 790.53 |
| 308.15 | 30000.00 | 787.05 |
| 313.15 | 30000.00 | 783.59 |
| 318.15 | 30000.00 | 780.14 |
| 323.15 | 30000.00 | 776.74 |
| 328.15 | 30000.00 | 773.28 |
| 333.15 | 30000.00 | 769.84 |
| 283.15 | 35000.00 | 807.58 |
| 288.15 | 35000.00 | 804.15 |
| 293.15 | 35000.00 | 800.71 |
| 298.15 | 35000.00 | 797.31 |
| 303.15 | 35000.00 | 793.91 |
| 308.15 | 35000.00 | 790.52 |
| 313.15 | 35000.00 | 787.12 |
| 318.15 | 35000.00 | 783.75 |
| 323.15 | 35000.00 | 780.43 |
| 328.15 | 35000.00 | 777.06 |
| 333.15 | 35000.00 | 773.7 |
| 283.15 | 40000.00 | 810.61 |
| 288.15 | 40000.00 | 807.23 |
| 293.15 | 40000.00 | 803.86 |
| 298.15 | 40000.00 | 800.51 |
| 303.15 | 40000.00 | 797.19 |
| 308.15 | 40000.00 | 793.86 |
| 313.15 | 40000.00 | 790.53 |
| 318.15 | 40000.00 | 787.22 |
| 323.15 | 40000.00 | 783.97 |
| 328.15 | 40000.00 | 780.66 |
| 333.15 | 40000.00 | 777.39 |
| 283.15 | 45000.00 | 813.52 |
| 288.15 | 45000.00 | 810.19 |
| 293.15 | 45000.00 | 806.9 |
| 298.15 | 45000.00 | 803.61 |
| 303.15 | 45000.00 | 800.34 |
| 308.15 | 45000.00 | 797.07 |
| 313.15 | 45000.00 | 793.81 |
| 318.15 | 45000.00 | 790.57 |
| 323.15 | 45000.00 | 787.37 |
| 328.15 | 45000.00 | 784.15 |
| 333.15 | 45000.00 | 780.93 |
| 283.15 | 50000.00 | 816.37 |
| 288.15 | 50000.00 | 813.09 |
| 293.15 | 50000.00 | 809.84 |
| 298.15 | 50000.00 | 806.62 |
| 303.15 | 50000.00 | 803.4 |
| 308.15 | 50000.00 | 800.19 |
| 313.15 | 50000.00 | 796.97 |
| 318.15 | 50000.00 | 793.81 |
| 323.15 | 50000.00 | 790.66 |
| 328.15 | 50000.00 | 787.49 |
| 333.15 | 50000.00 | 784.33 |
| 283.15 | 55000.00 | 819.14 |
| 288.15 | 55000.00 | 815.91 |
| 293.15 | 55000.00 | 812.71 |
| 298.15 | 55000.00 | 809.51 |
| 303.15 | 55000.00 | 806.36 |
| 308.15 | 55000.00 | 803.2 |
| 313.15 | 55000.00 | 800.03 |
| 318.15 | 55000.00 | 796.91 |
| 323.15 | 55000.00 | 793.83 |
| 328.15 | 55000.00 | 790.7 |
| 333.15 | 55000.00 | 787.59 |
| 283.15 | 60000.00 | 821.82 |
| 288.15 | 60000.00 | 818.64 |
| 293.15 | 60000.00 | 815.48 |
| 298.15 | 60000.00 | 812.33 |
| 303.15 | 60000.00 | 809.23 |
| 308.15 | 60000.00 | 806.11 |
| 313.15 | 60000.00 | 803.0 |
| 318.15 | 60000.00 | 799.93 |
| 323.15 | 60000.00 | 796.89 |
| 328.15 | 60000.00 | 793.83 |
| 333.15 | 60000.00 | 790.76 |
| 283.15 | 65000.00 | 824.44 |
| 288.15 | 65000.00 | 821.33 |
| 293.15 | 65000.00 | 818.18 |
| 298.15 | 65000.00 | 815.07 |
| 303.15 | 65000.00 | 812.01 |
| 308.15 | 65000.00 | 808.94 |
| 313.15 | 65000.00 | 805.88 |
| 318.15 | 65000.00 | 802.85 |
| 323.15 | 65000.00 | 799.86 |
| 328.15 | 65000.00 | 796.84 |
| 333.15 | 65000.00 | 793.83 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [336.92; 471.74] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54424e+01 | |||
| Coefficient B | -4.12026e+03 | |||
| Coefficient C | -6.50410e+01 | |||
| Temperature range, min. | 336.92 | |||
| Temperature range, max. | 471.74 | |||
| Pvap | 1.33 | kPa | 336.92 | Calculated Property |
| Pvap | 2.94 | kPa | 351.90 | Calculated Property |
| Pvap | 6.00 | kPa | 366.88 | Calculated Property |
| Pvap | 11.44 | kPa | 381.86 | Calculated Property |
| Pvap | 20.58 | kPa | 396.84 | Calculated Property |
| Pvap | 35.19 | kPa | 411.82 | Calculated Property |
| Pvap | 57.56 | kPa | 426.80 | Calculated Property |
| Pvap | 90.53 | kPa | 441.78 | Calculated Property |
| Pvap | 137.54 | kPa | 456.76 | Calculated Property |
| Pvap | 202.63 | kPa | 471.74 | Calculated Property |
| Pvap | [0.06; 71.03] | kPa | [287.15; 433.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 2.00294e+02 | |||
| Coefficient B | -1.37408e+04 | |||
| Coefficient C | -2.77392e+01 | |||
| Coefficient D | 2.18467e-05 | |||
| Temperature range, min. | 287.15 | |||
| Temperature range, max. | 433.15 | |||
| Pvap | 0.06 | kPa | 287.15 | Calculated Property |
| Pvap | 0.22 | kPa | 303.37 | Calculated Property |
| Pvap | 0.64 | kPa | 319.59 | Calculated Property |
| Pvap | 1.64 | kPa | 335.82 | Calculated Property |
| Pvap | 3.72 | kPa | 352.04 | Calculated Property |
| Pvap | 7.68 | kPa | 368.26 | Calculated Property |
| Pvap | 14.65 | kPa | 384.48 | Calculated Property |
| Pvap | 26.13 | kPa | 400.71 | Calculated Property |
| Pvap | 44.10 | kPa | 416.93 | Calculated Property |
| Pvap | 71.03 | kPa | 433.15 | Calculated Property |
Similar Compounds
![2-[2-(2-Isopentoxyethoxy)ethoxy]ethanol.](data:image/png;base64,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)
Find more compounds similar to Diisoamyl ether.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Experimental and modeled volumetric behavior of linear and branched ethers
- 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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.