- 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
- Isoamyl ether
- Isoamyl oxide
- Isopentyl ether
- NSC 9281
- bis(3-methylbutyl) ether
- bis(3-methylbutyl)ether
- di-(3-methylbutyl) ether
- diisopentyl ether
- ether, diisoamyl
- ether, diisopentyl
- ω : Acentric Factor.
- 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).
- 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).
- 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 |
|---|---|---|---|
| ω | 0.5036 | Relay (1.0) Calculated Property | |
| ΔfG° | -76.56 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -408.29 | kJ/mol | Relay (1.0) 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 |
| IE | 9.30 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.49 | Relay (1.0) 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 | |
| I | 1063.00 | 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 | 619.99 | K | Relay (1.0) Calculated Property |
| Tfus | 187.13 | K | Relay (1.0) Calculated Property |
| Vc | 0.589 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| 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 |
|---|---|---|---|---|
| Cp,gas | [232.39; 554.81] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.59340e+01 | |||
| Coefficient B | 9.02480e-01 | |||
| Coefficient C | -4.15600e-04 | |||
| Coefficient D | 5.20000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 232.39 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 285.50 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 333.90 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 377.76 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 417.24 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 452.52 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 483.75 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 511.10 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 534.73 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 554.81 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0125876; 0.0002079] | Pa×s | [194.69; 433.67] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.18216e+01 | |||
| Coefficient B | 1.44977e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 194.69 | |||
| Temperature range, max. | 433.67 | |||
| η | 0.0125876 | Pa×s | 194.69 | Calculated Property |
| η | 0.0051500 | Pa×s | 221.24 | Calculated Property |
| η | 0.0025518 | Pa×s | 247.80 | Calculated Property |
| η | 0.0014485 | Pa×s | 274.35 | Calculated Property |
| η | 0.0009087 | Pa×s | 300.90 | Calculated Property |
| η | 0.0006148 | Pa×s | 327.46 | Calculated Property |
| η | 0.0004411 | Pa×s | 354.01 | Calculated Property |
| η | 0.0003314 | Pa×s | 380.56 | Calculated Property |
| η | 0.0002585 | Pa×s | 407.11 | Calculated Property |
| η | 0.0002079 | Pa×s | 433.67 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [336.92; 471.74] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.00294e+02 | |||
| Coefficient B | -1.37408e+04 | |||
| Coefficient C | -2.77392e+01 | |||
| Coefficient D | 2.18467e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| 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 |
| Pvap | [0.13; 101.45] | kPa | [291.80; 446.60] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.55116e+01 | |||
| Coefficient B | -4.45682e+03 | |||
| Coefficient C | -3.74170e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 291.80 | |||
| Temperature range, max. | 446.60 | |||
| Pvap | 0.13 | kPa | 291.80 | Calculated Property |
| Pvap | 0.41 | kPa | 309.00 | Calculated Property |
| Pvap | 1.08 | kPa | 326.20 | Calculated Property |
| Pvap | 2.58 | kPa | 343.40 | Calculated Property |
| Pvap | 5.59 | kPa | 360.60 | Calculated Property |
| Pvap | 11.22 | kPa | 377.80 | Calculated Property |
| Pvap | 21.07 | kPa | 395.00 | Calculated Property |
| Pvap | 37.33 | kPa | 412.20 | Calculated Property |
| Pvap | 62.91 | kPa | 429.40 | Calculated Property |
| Pvap | 101.45 | kPa | 446.60 | 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
- Cheméo Relay (1.0)
- 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
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