- Name
- Ethanol, 2-butoxy-
- InChI
- InChI=1S/C6H14O2/c1-2-3-5-8-6-4-7/h7H,2-6H2,1H3
- InChI Key
- POAOYUHQDCAZBD-UHFFFAOYSA-N
- Formula
- C6H14O2
- SMILES
- CCCCOCCO
- Mol. Weight (g/mol)
- 118.17
- CAS
- 111-76-2
- Name
- Cyclohexane
- InChI
- InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
- InChI Key
- XDTMQSROBMDMFD-UHFFFAOYSA-N
- Formula
- C6H12
- SMILES
- C1CCCCC1
- Mol. Weight (g/mol)
- 84.16
- CAS
- 110-82-7
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Datasets
- η - Viscosity, Pa*s (2)
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
- csound,fluid - Speed of Sound, m/s (2)
- Tfus - Solid-liquid equilibrium temperature, K (2)
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0557 | 0.0009 |
| 298.15 | 0.1501 | 0.0010 |
| 298.15 | 0.2504 | 0.0012 |
| 298.15 | 0.3543 | 0.0013 |
| 298.15 | 0.4488 | 0.0014 |
| 298.15 | 0.5025 | 0.0015 |
| 298.15 | 0.5493 | 0.0016 |
| 298.15 | 0.6485 | 0.0018 |
| 298.15 | 0.7494 | 0.0020 |
| 298.15 | 0.8511 | 0.0023 |
| 298.15 | 0.9556 | 0.0026 |
| 308.15 | 0.0557 | 0.0008 |
| 308.15 | 0.1501 | 0.0009 |
| 308.15 | 0.2504 | 0.0010 |
| 308.15 | 0.3543 | 0.0011 |
| 308.15 | 0.4488 | 0.0012 |
| 308.15 | 0.5025 | 0.0012 |
| 308.15 | 0.5493 | 0.0013 |
| 308.15 | 0.6485 | 0.0015 |
| 308.15 | 0.7494 | 0.0016 |
| 308.15 | 0.8511 | 0.0018 |
| 308.15 | 0.9556 | 0.0021 |
Viscosity, Pa*s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 0.0557 | 0.0009 |
| 298.15 | 0.1501 | 0.0010 |
| 298.15 | 0.2504 | 0.0012 |
| 298.15 | 0.3543 | 0.0013 |
| 298.15 | 0.4488 | 0.0014 |
| 298.15 | 0.5025 | 0.0015 |
| 298.15 | 0.5493 | 0.0016 |
| 298.15 | 0.6485 | 0.0018 |
| 298.15 | 0.7494 | 0.0020 |
| 298.15 | 0.8511 | 0.0023 |
| 298.15 | 0.9556 | 0.0026 |
| 308.15 | 0.0557 | 0.0008 |
| 308.15 | 0.1501 | 0.0009 |
| 308.15 | 0.2504 | 0.0010 |
| 308.15 | 0.3543 | 0.0011 |
| 308.15 | 0.4488 | 0.0012 |
| 308.15 | 0.5025 | 0.0012 |
| 308.15 | 0.5493 | 0.0013 |
| 308.15 | 0.6485 | 0.0015 |
| 308.15 | 0.7494 | 0.0016 |
| 308.15 | 0.8511 | 0.0018 |
| 308.15 | 0.9556 | 0.0021 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Cyclohexane (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0414 | 0.4171 |
| 0.0836 | 0.6245 |
| 0.1265 | 0.7657 |
| 0.1702 | 0.8662 |
| 0.2148 | 0.9297 |
| 0.2602 | 0.9757 |
| 0.3065 | 1.005 |
| 0.3536 | 1.016 |
| 0.4017 | 1.011 |
| 0.4507 | 0.9968 |
| 0.5007 | 0.9593 |
| 0.5518 | 0.9153 |
| 0.6038 | 0.8531 |
| 0.6569 | 0.7800 |
| 0.7111 | 0.6887 |
| 0.7665 | 0.5819 |
| 0.8230 | 0.4599 |
| 0.8807 | 0.3223 |
| 0.9397 | 0.1681 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 313.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Cyclohexane (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0414 | 0.4171 |
| 0.0836 | 0.6245 |
| 0.1265 | 0.7657 |
| 0.1702 | 0.8662 |
| 0.2148 | 0.9297 |
| 0.2602 | 0.9757 |
| 0.3065 | 1.005 |
| 0.3536 | 1.016 |
| 0.4017 | 1.011 |
| 0.4507 | 0.9968 |
| 0.5007 | 0.9593 |
| 0.5518 | 0.9153 |
| 0.6038 | 0.8531 |
| 0.6569 | 0.7800 |
| 0.7111 | 0.6887 |
| 0.7665 | 0.5819 |
| 0.8230 | 0.4599 |
| 0.8807 | 0.3223 |
| 0.9397 | 0.1681 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0557 | 780.53 |
| 298.15 | 0.1501 | 792.14 |
| 298.15 | 0.2504 | 804.78 |
| 298.15 | 0.3543 | 818.03 |
| 298.15 | 0.4488 | 830.1 |
| 298.15 | 0.5025 | 836.93 |
| 298.15 | 0.5493 | 842.84 |
| 298.15 | 0.6485 | 855.22 |
| 298.15 | 0.7494 | 867.52 |
| 298.15 | 0.8511 | 879.52 |
| 298.15 | 0.9556 | 891.37 |
| 303.15 | 0.0557 | 774.84 |
| 303.15 | 0.1501 | 786.38 |
| 303.15 | 0.2504 | 799.25 |
| 303.15 | 0.3543 | 812.87 |
| 303.15 | 0.4488 | 825.26 |
| 303.15 | 0.5025 | 832.23 |
| 303.15 | 0.5493 | 838.24 |
| 303.15 | 0.6485 | 850.72 |
| 303.15 | 0.7494 | 863.02 |
| 303.15 | 0.8511 | 875.01 |
| 303.15 | 0.9556 | 887.0 |
| 308.15 | 0.0557 | 771.17 |
| 308.15 | 0.1501 | 782.85 |
| 308.15 | 0.2504 | 795.54 |
| 308.15 | 0.3543 | 808.84 |
| 308.15 | 0.4488 | 820.97 |
| 308.15 | 0.5025 | 827.84 |
| 308.15 | 0.5493 | 833.8 |
| 308.15 | 0.6485 | 846.33 |
| 308.15 | 0.7494 | 858.87 |
| 308.15 | 0.8511 | 871.26 |
| 308.15 | 0.9556 | 883.7 |
| 313.15 | 0.0557 | 765.44 |
| 313.15 | 0.1501 | 776.71 |
| 313.15 | 0.2504 | 789.54 |
| 313.15 | 0.3543 | 803.16 |
| 313.15 | 0.4488 | 815.49 |
| 313.15 | 0.5025 | 822.38 |
| 313.15 | 0.5493 | 828.29 |
| 313.15 | 0.6485 | 840.55 |
| 313.15 | 0.7494 | 852.71 |
| 313.15 | 0.8511 | 864.88 |
| 313.15 | 0.9556 | 877.7 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 0.0557 | 780.53 |
| 298.15 | 0.1501 | 792.14 |
| 298.15 | 0.2504 | 804.78 |
| 298.15 | 0.3543 | 818.03 |
| 298.15 | 0.4488 | 830.1 |
| 298.15 | 0.5025 | 836.93 |
| 298.15 | 0.5493 | 842.84 |
| 298.15 | 0.6485 | 855.22 |
| 298.15 | 0.7494 | 867.52 |
| 298.15 | 0.8511 | 879.52 |
| 298.15 | 0.9556 | 891.37 |
| 303.15 | 0.0557 | 774.84 |
| 303.15 | 0.1501 | 786.38 |
| 303.15 | 0.2504 | 799.25 |
| 303.15 | 0.3543 | 812.87 |
| 303.15 | 0.4488 | 825.26 |
| 303.15 | 0.5025 | 832.23 |
| 303.15 | 0.5493 | 838.24 |
| 303.15 | 0.6485 | 850.72 |
| 303.15 | 0.7494 | 863.02 |
| 303.15 | 0.8511 | 875.01 |
| 303.15 | 0.9556 | 887.0 |
| 308.15 | 0.0557 | 771.17 |
| 308.15 | 0.1501 | 782.85 |
| 308.15 | 0.2504 | 795.54 |
| 308.15 | 0.3543 | 808.84 |
| 308.15 | 0.4488 | 820.97 |
| 308.15 | 0.5025 | 827.84 |
| 308.15 | 0.5493 | 833.8 |
| 308.15 | 0.6485 | 846.33 |
| 308.15 | 0.7494 | 858.87 |
| 308.15 | 0.8511 | 871.26 |
| 308.15 | 0.9556 | 883.7 |
| 313.15 | 0.0557 | 765.44 |
| 313.15 | 0.1501 | 776.71 |
| 313.15 | 0.2504 | 789.54 |
| 313.15 | 0.3543 | 803.16 |
| 313.15 | 0.4488 | 815.49 |
| 313.15 | 0.5025 | 822.38 |
| 313.15 | 0.5493 | 828.29 |
| 313.15 | 0.6485 | 840.55 |
| 313.15 | 0.7494 | 852.71 |
| 313.15 | 0.8511 | 864.88 |
| 313.15 | 0.9556 | 877.7 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0557 | 1244.0 |
| 298.15 | 0.1501 | 1236.0 |
| 298.15 | 0.2504 | 1237.0 |
| 298.15 | 0.3543 | 1242.0 |
| 298.15 | 0.4488 | 1250.0 |
| 298.15 | 0.5025 | 1255.0 |
| 298.15 | 0.5493 | 1260.0 |
| 298.15 | 0.6485 | 1269.0 |
| 298.15 | 0.7494 | 1278.0 |
| 298.15 | 0.8511 | 1287.0 |
| 298.15 | 0.9556 | 1298.0 |
| 308.15 | 0.0557 | 1206.0 |
| 308.15 | 0.1501 | 1202.0 |
| 308.15 | 0.2504 | 1202.0 |
| 308.15 | 0.3543 | 1206.0 |
| 308.15 | 0.4488 | 1212.0 |
| 308.15 | 0.5025 | 1216.0 |
| 308.15 | 0.5493 | 1220.0 |
| 308.15 | 0.6485 | 1229.0 |
| 308.15 | 0.7494 | 1241.0 |
| 308.15 | 0.8511 | 1255.0 |
| 308.15 | 0.9556 | 1275.0 |
Speed of sound, m/s [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Speed of sound, m/s - Liquid |
| 298.15 | 0.0557 | 1244.0 |
| 298.15 | 0.1501 | 1236.0 |
| 298.15 | 0.2504 | 1237.0 |
| 298.15 | 0.3543 | 1242.0 |
| 298.15 | 0.4488 | 1250.0 |
| 298.15 | 0.5025 | 1255.0 |
| 298.15 | 0.5493 | 1260.0 |
| 298.15 | 0.6485 | 1269.0 |
| 298.15 | 0.7494 | 1278.0 |
| 298.15 | 0.8511 | 1287.0 |
| 298.15 | 0.9556 | 1298.0 |
| 308.15 | 0.0557 | 1206.0 |
| 308.15 | 0.1501 | 1202.0 |
| 308.15 | 0.2504 | 1202.0 |
| 308.15 | 0.3543 | 1206.0 |
| 308.15 | 0.4488 | 1212.0 |
| 308.15 | 0.5025 | 1216.0 |
| 308.15 | 0.5493 | 1220.0 |
| 308.15 | 0.6485 | 1229.0 |
| 308.15 | 0.7494 | 1241.0 |
| 308.15 | 0.8511 | 1255.0 |
| 308.15 | 0.9556 | 1275.0 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 279.96 |
| 0.0529 | 274.49 |
| 0.1021 | 271.72 |
| 0.1501 | 269.45 |
| 0.2005 | 267.16 |
| 0.2508 | 264.61 |
| 0.2974 | 262.51 |
| 0.3038 | 262.45 |
| 0.3516 | 259.20 |
| 0.4009 | 255.85 |
| 0.4494 | 251.19 |
| 0.5012 | 246.44 |
| 0.5532 | 240.34 |
| 0.6000 | 233.99 |
| 0.6502 | 225.38 |
| 0.6997 | 216.22 |
Solid-liquid equilibrium temperature, K [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Mole fraction of Ethanol, 2-butoxy- (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
|---|---|
| 0.0000 | 279.96 |
| 0.0529 | 274.49 |
| 0.1021 | 271.72 |
| 0.1501 | 269.45 |
| 0.2005 | 267.16 |
| 0.2508 | 264.61 |
| 0.2974 | 262.51 |
| 0.3038 | 262.45 |
| 0.3516 | 259.20 |
| 0.4009 | 255.85 |
| 0.4494 | 251.19 |
| 0.5012 | 246.44 |
| 0.5532 | 240.34 |
| 0.6000 | 233.99 |
| 0.6502 | 225.38 |
| 0.6997 | 216.22 |
Sources
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
- Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
- Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol