- InChI
- InChI=1S/C6H14O/c1-3-5-7-6-4-2/h3-6H2,1-2H3
- InChI Key
- POLCUAVZOMRGSN-UHFFFAOYSA-N
- Formula
- C6H14O
- SMILES
- CCCOCCC
- Molecular Weight1
- 102.17
- CAS
- 111-43-3
- Other Names
-
- (n-C3H7)2O
- 1,1'-OXYBIS PROPANE
- 1,1'-Oxybis[propane]
- 1-propoxypropane
- 4-Oxaheptane
- Dipropyl ether
- Dipropyl oxide
- Ether, di-n-propyl-
- Propane, 1,1'-oxybis-
- Propyl ether
- UN 2384
- n-Propyl ether
- ω : Acentric Factor.
- 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).
- μ : Dipole Moment (debye).
- 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.
- I : Polar retention indices.
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3690 | KDB | |
| PAff | 837.90 | kJ/mol | NIST |
| BasG | 810.50 | kJ/mol | NIST |
| ΔcH°liquid | [-4033.10; -4028.90] | kJ/mol |
|
| ΔcH°liquid | -4033.10 ± 0.79 | kJ/mol | NIST |
| ΔcH°liquid | -4028.90 ± 2.10 | kJ/mol | NIST |
| μ | 1.20 | debye | KDB |
| ΔfG° | -105.60 | kJ/mol | KDB |
| ΔfH°gas | [-299.00; -293.00] | kJ/mol |
|
| ΔfH°gas | -293.10 | kJ/mol | KDB |
| ΔfH°gas | -293.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°gas | -299.00 | kJ/mol | NIST |
| ΔfH°liquid | [-333.10; -328.80] | kJ/mol |
|
| ΔfH°liquid | -328.80 ± 0.88 | kJ/mol | NIST |
| ΔfH°liquid | -333.10 ± 2.10 | kJ/mol | NIST |
| ΔfusH° | 12.48 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [35.68; 36.50] | kJ/mol |
|
| ΔvapH° | 35.79 | kJ/mol | NIST |
| ΔvapH° | 35.68 | kJ/mol | NIST |
| ΔvapH° | 35.70 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 36.50 ± 1.30 | kJ/mol | NIST |
| IE | [9.27; 9.53] | eV |
|
| IE | 9.30 ± 0.03 | eV | NIST |
| IE | 9.32 ± 0.01 | eV | NIST |
| IE | 9.27 ± 0.05 | eV | NIST |
| IE | 9.53 | eV | NIST |
| IE | 9.49 | eV | NIST |
| log10WS | [-1.62; -1.62] |
|
|
| log10WS | -1.62 | Aq. Sol... | |
| log10WS | -1.62 | Estimat... | |
| logPoct/wat | 1.823 | Crippen Calculated Property | |
| McVol | 101.270 | ml/mol | McGowan Calculated Property |
| Pc | [3028.00; 3028.00] | kPa |
|
| Pc | 3028.00 | kPa | KDB |
| Pc | 3028.00 ± 6.00 | kPa | NIST |
| Inp | [656.00; 691.00] |
|
|
| Inp | 656.00 | NIST | |
| Inp | 656.80 | NIST | |
| Inp | 657.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | Outlier 691.00 | NIST | |
| Inp | 656.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 659.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 656.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 680.00 | NIST | |
| I | [766.00; 794.00] |
|
|
| I | 773.00 | NIST | |
| I | Outlier 794.00 | NIST | |
| I | 775.00 | NIST | |
| I | 768.00 | NIST | |
| I | 775.00 | NIST | |
| I | 770.00 | NIST | |
| I | 769.00 | NIST | |
| I | 769.00 | NIST | |
| I | 774.00 | NIST | |
| I | 770.00 | NIST | |
| I | 777.00 | NIST | |
| I | 777.00 | NIST | |
| I | 766.00 | NIST | |
| I | 782.00 | NIST | |
| I | 773.00 | NIST | |
| I | 770.00 | NIST | |
| S°gas | 422.50 | J/mol×K | NIST |
| S°liquid | 323.90 | J/mol×K | NIST |
| Tboil | [362.20; 364.20] | K |
|
| Tboil | 363.23 | K | KDB |
| Tboil | 363.23 | K | (Liquid... |
| Tboil | 363.16 | K | Isobari... |
| Tboil | 362.87 | K | Vapor L... |
| Tboil | Outlier 362.20 | K | NIST |
| Tboil | 364.20 | K | NIST |
| Tboil | 363.10 | K | NIST |
| Tboil | 363.26 ± 0.10 | K | NIST |
| Tboil | 364.15 ± 0.50 | K | NIST |
| Tboil | 363.90 ± 1.00 | K | NIST |
| Tboil | 363.30 ± 0.50 | K | NIST |
| Tc | [530.60; 530.60] | K |
|
| Tc | 530.60 | K | KDB |
| Tc | 530.60 | K | NIST |
| Tc | 530.60 ± 0.30 | K | NIST |
| Tfus | [147.00; 149.95] | K |
|
| Tfus | 147.00 | K | KDB |
| Tfus | 149.95 ± 0.40 | K | NIST |
| Ttriple | [149.40; 158.36] | K |
|
| Ttriple | 158.36 | K | KDB |
| Ttriple | 149.40 ± 0.10 | K | NIST |
| Ttriple | 158.36 ± 0.06 | K | NIST |
| Vc | 0.390 | m3/kmol | KDB |
| Zc | 0.2673370 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [182.95; 221.05] | J/mol×K | [360.00; 460.01] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 400 450 | ||||
| Cp,gas | 182.95 | J/mol×K | 360.00 | NIST |
| Cp,gas | 190.77 | J/mol×K | 380.01 | NIST |
| Cp,gas | 198.45 | J/mol×K | 399.98 | NIST |
| Cp,gas | 209.91 | J/mol×K | 430.05 | NIST |
| Cp,gas | 221.05 | J/mol×K | 460.01 | NIST |
| Cp,liquid | [221.45; 221.60] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 221.45 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 221.60 | J/mol×K | 298.15 | NIST |
| η | [0.0002210; 0.0035470] | Pa×s | [179.61; 359.10] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 200 250 300 350 | ||||
| η | 0.0035470 | Pa×s | 179.61 | Joback Calculated Property |
| η | 0.0016051 | Pa×s | 209.53 | Joback Calculated Property |
| η | 0.0008855 | Pa×s | 239.44 | Joback Calculated Property |
| η | 0.0005575 | Pa×s | 269.36 | Joback Calculated Property |
| η | 0.0003850 | Pa×s | 299.27 | Joback Calculated Property |
| η | 0.0002844 | Pa×s | 329.19 | Joback Calculated Property |
| η | 0.0002210 | Pa×s | 359.10 | Joback Calculated Property |
| ΔfusH | 10.77 | kJ/mol | 158.40 | NIST |
| ΔvapH | [31.27; 35.60] | kJ/mol | [323.00; 497.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 31 32 33 34 35 36 350 400 450 500 | ||||
| ΔvapH | 34.80 | kJ/mol | 323.00 | NIST |
| ΔvapH | 35.10 | kJ/mol | 331.00 | NIST |
| ΔvapH | 35.60 | kJ/mol | 340.50 | NIST |
| ΔvapH | 34.60 | kJ/mol | 341.50 | NIST |
| ΔvapH | 34.50 | kJ/mol | 359.50 | NIST |
| ΔvapH | 31.40 | kJ/mol | 363.00 | NIST |
| ΔvapH | 31.31 | kJ/mol | 363.10 | NIST |
| ΔvapH | 34.43 | kJ/mol | 363.20 | KDB |
| ΔvapH | 31.27 | kJ/mol | 363.22 | NIST |
| ΔvapH | 32.20 | kJ/mol | 426.00 | NIST |
| ΔvapH | 32.40 | kJ/mol | 497.50 | NIST |
| Pvap | [29.35; 135.50] | kPa | [326.73; 373.15] |
|
|
T(K) Vapor pressure (kPa) 20 40 60 80 100 120 140 340 360 | ||||
| Pvap | 29.35 | kPa | 326.73 | Vapor L... |
| Pvap | 36.71 | kPa | 332.57 | Vapor L... |
| Pvap | 42.54 | kPa | 336.55 | Vapor L... |
| Pvap | 49.98 | kPa | 341.15 | Vapor L... |
| Pvap | 57.75 | kPa | 345.34 | Vapor L... |
| Pvap | 60.00 | kPa | 346.55 | Vapor L... |
| Pvap | 60.00 | kPa | 346.63 | Vapor L... |
| Pvap | 62.30 | kPa | 347.55 | Vapor L... |
| Pvap | 72.36 | kPa | 352.11 | Vapor L... |
| Pvap | 74.10 | kPa | 353.15 | Thermod... |
| Pvap | 78.97 | kPa | 354.82 | Vapor L... |
| Pvap | 84.25 | kPa | 356.85 | Vapor L... |
| Pvap | 89.30 | kPa | 358.73 | Vapor L... |
| Pvap | 96.32 | kPa | 361.18 | Vapor L... |
| Pvap | 101.30 | kPa | 362.87 | Vapor L... |
| Pvap | 135.50 | kPa | 373.15 | Thermod... |
| n0 | [1.37840; 1.37840] | [298.15; 298.15] |
|
|
|
T(K) Refractive Index 1.25 1.3 1.35 1.4 1.45 1.5 | ||||
| n0 | 1.37840 | 298.15 | Isobari... | |
| n0 | 1.37840 | 298.15 | Vapor l... | |
| n0 | 1.37840 | 298.15 | Phase e... | |
| n0 | 1.37840 | 298.15 | Liquid ... | |
| n0 | 1.37840 | 298.15 | Isobari... | |
| n0 | 1.37840 | 298.15 | Phase E... | |
| ρl | [684.92; 742.00] | kg/m3 | [293.00; 358.15] |
|
|
T(K) Liquid Density (kg/m3) 680 690 700 710 720 730 740 300 320 340 | ||||
| ρl | 736.00 | kg/m3 | 293.00 | KDB |
| ρl | 741.94 | kg/m3 | 298.15 | Volumet... |
| ρl | 741.98 | kg/m3 | 298.15 | Excess ... |
| ρl | 742.00 | kg/m3 | 298.15 | Excess ... |
| ρl | 727.87 | kg/m3 | 313.15 | Volumet... |
| ρl | 713.73 | kg/m3 | 328.15 | Volumet... |
| ρl | 699.61 | kg/m3 | 343.15 | Volumet... |
| ρl | 684.92 | kg/m3 | 358.15 | Volumet... |
| γ | 0.02 | N/m | 298.20 | KDB |
| ΔvapS | 86.10 | J/mol×K | 363.22 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 757.39 |
| 288.15 | 100.00 | 752.52 |
| 293.15 | 100.00 | 747.63 |
| 298.15 | 100.00 | 742.71 |
| 303.15 | 100.00 | 737.77 |
| 308.15 | 100.00 | 732.8 |
| 313.15 | 100.00 | 727.8 |
| 318.15 | 100.00 | 722.77 |
| 323.15 | 100.00 | 717.7 |
| 328.15 | 100.00 | 712.59 |
| 333.15 | 100.00 | 707.45 |
| 283.15 | 5000.00 | 762.38 |
| 288.15 | 5000.00 | 757.69 |
| 293.15 | 5000.00 | 752.98 |
| 298.15 | 5000.00 | 748.24 |
| 303.15 | 5000.00 | 743.49 |
| 308.15 | 5000.00 | 738.69 |
| 313.15 | 5000.00 | 733.9 |
| 318.15 | 5000.00 | 729.04 |
| 323.15 | 5000.00 | 724.25 |
| 328.15 | 5000.00 | 719.28 |
| 333.15 | 5000.00 | 714.57 |
| 283.15 | 10000.00 | 767.05 |
| 288.15 | 10000.00 | 762.5 |
| 293.15 | 10000.00 | 757.94 |
| 298.15 | 10000.00 | 753.37 |
| 303.15 | 10000.00 | 748.78 |
| 308.15 | 10000.00 | 744.18 |
| 313.15 | 10000.00 | 739.57 |
| 318.15 | 10000.00 | 735.01 |
| 323.15 | 10000.00 | 730.31 |
| 328.15 | 10000.00 | 725.68 |
| 333.15 | 10000.00 | 721.03 |
| 283.15 | 15000.00 | 771.45 |
| 288.15 | 15000.00 | 767.01 |
| 293.15 | 15000.00 | 762.58 |
| 298.15 | 15000.00 | 758.15 |
| 303.15 | 15000.00 | 753.68 |
| 308.15 | 15000.00 | 749.22 |
| 313.15 | 15000.00 | 744.77 |
| 318.15 | 15000.00 | 740.33 |
| 323.15 | 15000.00 | 735.84 |
| 328.15 | 15000.00 | 731.37 |
| 333.15 | 15000.00 | 726.88 |
| 283.15 | 20000.00 | 775.62 |
| 288.15 | 20000.00 | 771.21 |
| 293.15 | 20000.00 | 766.89 |
| 298.15 | 20000.00 | 762.57 |
| 303.15 | 20000.00 | 758.26 |
| 308.15 | 20000.00 | 753.95 |
| 313.15 | 20000.00 | 749.62 |
| 318.15 | 20000.00 | 745.32 |
| 323.15 | 20000.00 | 741.0 |
| 328.15 | 20000.00 | 736.67 |
| 333.15 | 20000.00 | 732.34 |
| 283.15 | 25000.00 | 779.52 |
| 288.15 | 25000.00 | 775.22 |
| 293.15 | 25000.00 | 771.01 |
| 298.15 | 25000.00 | 766.81 |
| 303.15 | 25000.00 | 762.61 |
| 308.15 | 25000.00 | 758.41 |
| 313.15 | 25000.00 | 754.2 |
| 318.15 | 25000.00 | 750.04 |
| 323.15 | 25000.00 | 745.84 |
| 328.15 | 25000.00 | 741.66 |
| 333.15 | 25000.00 | 737.47 |
| 283.15 | 30000.00 | 783.28 |
| 288.15 | 30000.00 | 779.05 |
| 293.15 | 30000.00 | 774.94 |
| 298.15 | 30000.00 | 770.85 |
| 303.15 | 30000.00 | 766.76 |
| 308.15 | 30000.00 | 762.65 |
| 313.15 | 30000.00 | 758.55 |
| 318.15 | 30000.00 | 754.51 |
| 323.15 | 30000.00 | 750.43 |
| 328.15 | 30000.00 | 746.37 |
| 333.15 | 30000.00 | 742.3 |
| 283.15 | 35000.00 | 786.9 |
| 288.15 | 35000.00 | 782.73 |
| 293.15 | 35000.00 | 778.69 |
| 298.15 | 35000.00 | 774.71 |
| 303.15 | 35000.00 | 770.7 |
| 308.15 | 35000.00 | 766.7 |
| 313.15 | 35000.00 | 762.71 |
| 318.15 | 35000.00 | 758.76 |
| 323.15 | 35000.00 | 754.79 |
| 328.15 | 35000.00 | 750.85 |
| 333.15 | 35000.00 | 746.89 |
| 283.15 | 40000.00 | 790.38 |
| 288.15 | 40000.00 | 786.26 |
| 293.15 | 40000.00 | 782.3 |
| 298.15 | 40000.00 | 778.42 |
| 303.15 | 40000.00 | 774.48 |
| 308.15 | 40000.00 | 770.6 |
| 313.15 | 40000.00 | 766.68 |
| 318.15 | 40000.00 | 762.84 |
| 323.15 | 40000.00 | 758.96 |
| 328.15 | 40000.00 | 755.1 |
| 333.15 | 40000.00 | 751.24 |
| 283.15 | 45000.00 | 793.67 |
| 288.15 | 45000.00 | 789.68 |
| 293.15 | 45000.00 | 785.81 |
| 298.15 | 45000.00 | 781.98 |
| 303.15 | 45000.00 | 778.13 |
| 308.15 | 45000.00 | 774.31 |
| 313.15 | 45000.00 | 770.47 |
| 318.15 | 45000.00 | 766.72 |
| 323.15 | 45000.00 | 762.93 |
| 328.15 | 45000.00 | 759.16 |
| 333.15 | 45000.00 | 755.35 |
| 283.15 | 50000.00 | 796.87 |
| 288.15 | 50000.00 | 792.99 |
| 293.15 | 50000.00 | 789.18 |
| 298.15 | 50000.00 | 785.42 |
| 303.15 | 50000.00 | 781.64 |
| 308.15 | 50000.00 | 777.92 |
| 313.15 | 50000.00 | 774.17 |
| 318.15 | 50000.00 | 770.47 |
| 323.15 | 50000.00 | 766.76 |
| 328.15 | 50000.00 | 763.06 |
| 333.15 | 50000.00 | 759.32 |
| 283.15 | 55000.00 | 800.02 |
| 288.15 | 55000.00 | 796.16 |
| 293.15 | 55000.00 | 792.44 |
| 298.15 | 55000.00 | 788.74 |
| 303.15 | 55000.00 | 785.01 |
| 308.15 | 55000.00 | 781.37 |
| 313.15 | 55000.00 | 777.67 |
| 318.15 | 55000.00 | 774.07 |
| 323.15 | 55000.00 | 770.41 |
| 328.15 | 55000.00 | 766.79 |
| 333.15 | 55000.00 | 763.16 |
| 283.15 | 60000.00 | 802.99 |
| 288.15 | 60000.00 | 799.26 |
| 293.15 | 60000.00 | 795.56 |
| 298.15 | 60000.00 | 791.97 |
| 303.15 | 60000.00 | 788.28 |
| 308.15 | 60000.00 | 784.7 |
| 313.15 | 60000.00 | 781.06 |
| 318.15 | 60000.00 | 777.53 |
| 323.15 | 60000.00 | 773.95 |
| 328.15 | 60000.00 | 770.38 |
| 333.15 | 60000.00 | 766.84 |
| 283.15 | 65000.00 | 805.87 |
| 288.15 | 65000.00 | 802.29 |
| 293.15 | 65000.00 | 798.64 |
| 298.15 | 65000.00 | 795.06 |
| 303.15 | 65000.00 | 791.45 |
| 308.15 | 65000.00 | 787.86 |
| 313.15 | 65000.00 | 784.29 |
| 318.15 | 65000.00 | 780.73 |
| 323.15 | 65000.00 | 777.21 |
| 328.15 | 65000.00 | 773.71 |
| 333.15 | 65000.00 | 770.23 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [270.98; 385.07] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53894e+01 | |||
| Coefficient B | -3.45615e+03 | |||
| Coefficient C | -4.21280e+01 | |||
| Temperature range, min. | 270.98 | |||
| Temperature range, max. | 385.07 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| Pvap | 1.33 | kPa | 270.98 | Calculated Property |
| Pvap | 2.94 | kPa | 283.66 | Calculated Property |
| Pvap | 6.01 | kPa | 296.33 | Calculated Property |
| Pvap | 11.47 | kPa | 309.01 | Calculated Property |
| Pvap | 20.63 | kPa | 321.69 | Calculated Property |
| Pvap | 35.26 | kPa | 334.36 | Calculated Property |
| Pvap | 57.66 | kPa | 347.04 | Calculated Property |
| Pvap | 90.65 | kPa | 359.72 | Calculated Property |
| Pvap | 137.65 | kPa | 372.39 | Calculated Property |
| Pvap | 202.66 | kPa | 385.07 | Calculated Property |
| Pvap | [3.43e-07; 3017.14] | kPa | [149.95; 530.60] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.93819e+01 | |||
| Coefficient B | -7.55859e+03 | |||
| Coefficient C | -1.27960e+01 | |||
| Coefficient D | 1.12163e-05 | |||
| Temperature range, min. | 149.95 | |||
| Temperature range, max. | 530.60 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 500 | ||||
| Pvap | 3.43e-07 | kPa | 149.95 | Calculated Property |
| Pvap | 1.10e-03 | kPa | 192.24 | Calculated Property |
| Pvap | 0.13 | kPa | 234.54 | Calculated Property |
| Pvap | 2.67 | kPa | 276.83 | Calculated Property |
| Pvap | 21.38 | kPa | 319.13 | Calculated Property |
| Pvap | 96.01 | kPa | 361.42 | Calculated Property |
| Pvap | 299.56 | kPa | 403.72 | Calculated Property |
| Pvap | 739.50 | kPa | 446.01 | Calculated Property |
| Pvap | 1568.35 | kPa | 488.31 | Calculated Property |
| Pvap | 3017.14 | kPa | 530.60 | Calculated Property |
Similar Compounds
![CH3O[CH2CH2CH2O]3CH3.](data:image/png;base64,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)
Find more compounds similar to Di-n-propyl ether.
Mixtures
- 2-Pyrrolidinone, 1-methyl- + Di-n-propyl ether
- 1-Propanol + Di-n-propyl ether
- Di-n-propyl ether + 1-Pentanol
- 1-Propanol + Di-n-propyl ether + 1-Pentanol
- Di-n-propyl ether + Ethanol, 2-ethoxy-
- 1-Propanol + Di-n-propyl ether + Ethanol, 2-ethoxy-
- 1-Propanol + Di-n-propyl ether + Water
- 1-Propanol + 1,2-Ethanediol + Di-n-propyl ether
- Formamide, N,N-dimethyl- + Di-n-propyl ether
- Di-n-propyl ether + Propanoic acid + Water
- Di-n-propyl ether + Butane, 2,2-dimethyl-
- Di-n-propyl ether + Butane, 2,3-dimethyl-
- Di-n-propyl ether + Heptane
- Di-n-propyl ether + 1H-Imidazole
- Di-n-propyl ether + 1H-Imidazole, 2-methyl-
- Di-n-propyl ether + 1H-Imidazole, 1,2-dimethyl-
- Di-n-propyl ether + Octadecane
- Di-n-propyl ether + Nonadecane
- Eicosane + Di-n-propyl ether
- Tetracosane + Di-n-propyl ether
Find more mixtures with Di-n-propyl ether.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
- Thermodynamics of binary mixtures containing N-methyl-2-pyrrolidinone VLE measurements for systems with ethers Comparison with the Mod. UNIFAC (Do) and DISQUAC models Predictions for VLE, GE m, HEm and SLE?
- Experimental liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
- Isobaric vapor-liquid equilibria for the binary systems 1-propyl alcohol + dipropyl ether and 1-butyl alcohol + dibutyl ether at 20 and 101.3 kPa
- Vapor liquid equilibria in the ternary system dipropyl ether + 1-propanol + 1-pentanol and the binary systems dipropyl ether + 1-pentanol, 1-propanol + 1-pentanol at 101.3 kPa
- Phase equilibria involved in extractive distillation of dipropyl ether + 1-propyl alcohol using 2-ethoxyethanol as entrainer
- Liquid liquid equilibria of the systems dipropyl ether + n-propanol +water and dipropyl ether + n-propanol + ethylene glycol at different temperatures
- Thermodynamic study of perfluorohexane + ether mixtures VLE, LLE, and HE
- Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
- Liquid + liquid equilibria for the quaternary systems of (water + acetic acid + mixed solvent) at 298.2 K and atmospheric pressure
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- Experimental and modeled volumetric behavior of linear and branched ethers
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Volumetric properties of (N,N-dimethylformamide + aliphatic diethers) at Temperatures ranging from (298.15 to 358.15) K
- (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
- (Liquid + liquid) equilibria of (water + propionic acid + dipropyl ether or diisopropyl ether) at T = 298.2 K
- Isobaric (vapour + liquid + liquid) equilibrium data for (di-n-propyl ether + n-propyl alcohol + water) and (diisopropyl ether + isopropyl alcohol + water) systems at 100 kPa
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Excess molar enthalpies of ternary mixtures (dibutyl ether or dipropyl ether + 2,2-dimethylbutane + 2,3-dimethylbutane) at the temperature 298.15 K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
- Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
- Solubility of Imidazoles in Ethers
- Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
- Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Dipropyl Ether, 1-Propyl Alcohol, and Butyl Propionate
- Phase Equilibria Involved in Extractive Distillation of Dipropyl Ether + 1-Propyl Alcohol Using N,N-Dimethylformamide as Entrainer
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Excess Molar Enthalpies of Dipropyl Ether + Dibutyl Ether + (1-Hexene or Tetrahydrofuran) at 298.15 K
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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