- Name
- n-Butyl ether
- InChI
- InChI=1S/C8H18O/c1-3-5-7-9-8-6-4-2/h3-8H2,1-2H3
- InChI Key
- DURPTKYDGMDSBL-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCOCCCC
- Mol. Weight (g/mol)
- 130.23
- CAS
- 142-96-1
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
Datasets
Mole fraction of n-Butyl ether (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Butyl ether (1) - Liquid mixture 2 |
|---|---|
| 298.15 | 0.9925 |
| 318.15 | 0.9904 |
| 308.15 | 0.9898 |
Mole fraction of n-Butyl ether (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Butyl ether (1) - Liquid mixture 1 |
|---|---|
| 298.15 | 0.0001 |
| 318.15 | 0.0001 |
| 308.15 | 0.0001 |
Mole fraction of Water (2) [ref]
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
|---|---|
| 293.15 | 0.9999 |
| 298.15 | 0.9999 |
| 303.15 | 0.9998 |
| 308.15 | 0.9997 |
Mole fraction of Water (2) [ref]
Operational condition: Pressure, kPa = 100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 293.15 | 0.0063 |
| 298.15 | 0.0072 |
| 303.15 | 0.0099 |
| 308.15 | 0.0122 |
Mole fraction of n-Butyl ether (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Butyl ether (1) - Liquid mixture 1 |
|---|---|
| 288.15 | 0.9860 |
| 293.15 | 0.9832 |
| 298.15 | 0.9798 |
| 303.15 | 0.9749 |
| 308.15 | 0.9682 |
| 313.15 | 0.9628 |
| 318.15 | 0.9578 |
Mole fraction of n-Butyl ether (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of n-Butyl ether (1) - Liquid mixture 2 |
|---|---|
| 288.15 | 0.0000 |
| 293.15 | 0.0001 |
| 298.15 | 0.0003 |
| 303.15 | 0.0007 |
| 308.15 | 0.0011 |
| 313.15 | 0.0015 |
| 318.15 | 0.0020 |
Mole fraction of n-Butyl ether (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Butyl ether (1) - Liquid mixture 2 |
|---|---|
| 298.15 | 0.9925 |
| 318.15 | 0.9904 |
| 308.15 | 0.9898 |
Mole fraction of n-Butyl ether (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Butyl ether (1) - Liquid mixture 1 |
|---|---|
| 298.15 | 0.0001 |
| 318.15 | 0.0001 |
| 308.15 | 0.0001 |
Mole fraction of Water (2) [ref]
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
|---|---|
| 293.15 | 0.9999 |
| 298.15 | 0.9999 |
| 303.15 | 0.9998 |
| 308.15 | 0.9997 |
Mole fraction of Water (2) [ref]
Operational condition: Pressure, kPa = 100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 293.15 | 0.0063 |
| 298.15 | 0.0072 |
| 303.15 | 0.0099 |
| 308.15 | 0.0122 |
Mole fraction of n-Butyl ether (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of n-Butyl ether (1) - Liquid mixture 1 |
|---|---|
| 288.15 | 0.9860 |
| 293.15 | 0.9832 |
| 298.15 | 0.9798 |
| 303.15 | 0.9749 |
| 308.15 | 0.9682 |
| 313.15 | 0.9628 |
| 318.15 | 0.9578 |
Mole fraction of n-Butyl ether (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of n-Butyl ether (1) - Liquid mixture 2 |
|---|---|
| 288.15 | 0.0000 |
| 293.15 | 0.0001 |
| 298.15 | 0.0003 |
| 303.15 | 0.0007 |
| 308.15 | 0.0011 |
| 313.15 | 0.0015 |
| 318.15 | 0.0020 |
Sources
- (Liquid + liquid) equilibrium of (dibutyl ether + methanol + water) at different temperatures
- Ternary (liquid + liquid) equilibria for the extraction of ethanol, or 2-propanol from aqueous solutions with 1,1'-oxybis(butane) at different temperatures
- Binary Liquid-Liquid Equilibrium (LLE) for Dibutyl Ether (DBE) + Water from (288.15 to 318.15) K and Ternary LLE for Systems of DBE + C1 !less thanless than C4 Alcohols + Water at 298.15 K