Physical Properties
Property
Value
Unit
Source
ω
0.4000
KDB
μ
1.20
debye
KDB
Δf G°
-105.36
kJ/mol
Joback Calculated Property
Δf H°gas
-299.39
kJ/mol
Joback Calculated Property
Δfus H°
12.48
kJ/mol
Joback Calculated Property
Δvap H°
[36.30; 36.50]
kJ/mol
Δvap H°
36.41
kJ/mol
NIST
Δvap H°
36.30 ± 0.10
kJ/mol
NIST
Δvap H°
36.50
kJ/mol
NIST
IE
[9.30; 9.53]
eV
IE
9.30 ± 0.10
eV
NIST
IE
9.36
eV
NIST
IE
9.53
eV
NIST
log 10 WS
-1.42
Crippen Calculated Property
log Poct/wat
1.823
Crippen Calculated Property
McVol
101.270
ml/mol
McGowan Calculated Property
NFPA Fire
3
KDB
NFPA Health
2
KDB
Pc
3040.00
kPa
KDB
Inp
[648.00; 685.00]
Inp
669.00
NIST
Inp
665.00
NIST
Inp
669.00
NIST
Inp
668.00
NIST
Inp
684.00
NIST
Inp
684.00
NIST
Inp
Outlier 648.00
NIST
Inp
685.00
NIST
Inp
668.70
NIST
Inp
673.30
NIST
Inp
684.00
NIST
I
[780.00; 788.00]
I
780.00
NIST
I
788.00
NIST
I
788.00
NIST
I
780.00
NIST
Tboil
[364.70; 365.90]
K
Tboil
365.40
K
KDB
Tboil
365.25
K
Vapor L...
Tboil
364.70
K
NIST
Tboil
365.40
K
NIST
Tboil
365.20 ± 0.60
K
NIST
Tboil
365.50 ± 0.40
K
NIST
Tboil
365.90 ± 0.15
K
NIST
Tc
[531.00; 531.00]
K
Tc
531.00
K
KDB
Tc
531.00
K
NIST
Tfus
170.00
K
KDB
Vc
0.390
m3 /kmol
KDB
Zc
0.2685390
KDB
Temperature Dependent Properties
Datasets
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
100.00
759.63
288.15
100.00
754.84
293.15
100.00
750.02
298.15
100.00
745.17
303.15
100.00
740.3
308.15
100.00
735.39
313.15
100.00
730.45
318.15
100.00
725.44
323.15
100.00
720.43
328.15
100.00
715.37
333.15
100.00
710.26
283.15
5000.00
764.45
288.15
5000.00
759.82
293.15
5000.00
755.18
298.15
5000.00
750.51
303.15
5000.00
745.81
308.15
5000.00
741.09
313.15
5000.00
736.34
318.15
5000.00
731.57
323.15
5000.00
726.77
328.15
5000.00
721.95
333.15
5000.00
717.05
283.15
10000.00
768.96
288.15
10000.00
764.48
293.15
10000.00
759.98
298.15
10000.00
755.44
303.15
10000.00
750.9
308.15
10000.00
746.35
313.15
10000.00
741.76
318.15
10000.00
737.2
323.15
10000.00
732.59
328.15
10000.00
727.94
333.15
10000.00
723.28
283.15
15000.00
773.2
288.15
15000.00
768.83
293.15
15000.00
764.45
298.15
15000.00
760.05
303.15
15000.00
755.66
308.15
15000.00
751.24
313.15
15000.00
746.82
318.15
15000.00
742.41
323.15
15000.00
738.0
328.15
15000.00
733.52
333.15
15000.00
729.03
283.15
20000.00
777.2
288.15
20000.00
772.96
293.15
20000.00
768.69
298.15
20000.00
764.43
303.15
20000.00
760.15
308.15
20000.00
755.87
313.15
20000.00
751.59
318.15
20000.00
747.31
323.15
20000.00
743.03
328.15
20000.00
738.72
333.15
20000.00
734.4
283.15
25000.00
781.05
288.15
25000.00
776.9
293.15
25000.00
772.75
298.15
25000.00
768.58
303.15
25000.00
764.45
308.15
25000.00
760.26
313.15
25000.00
756.09
318.15
25000.00
751.96
323.15
25000.00
747.78
328.15
25000.00
743.64
333.15
25000.00
739.43
283.15
30000.00
784.72
288.15
30000.00
780.66
293.15
30000.00
776.62
298.15
30000.00
772.55
303.15
30000.00
768.49
308.15
30000.00
764.45
313.15
30000.00
760.38
318.15
30000.00
756.38
323.15
30000.00
752.29
328.15
30000.00
748.27
333.15
30000.00
744.2
283.15
35000.00
788.24
288.15
35000.00
784.28
293.15
35000.00
780.33
298.15
35000.00
776.36
303.15
35000.00
772.35
308.15
35000.00
768.44
313.15
35000.00
764.5
318.15
35000.00
760.54
323.15
35000.00
756.59
328.15
35000.00
752.68
333.15
35000.00
748.71
283.15
40000.00
791.65
288.15
40000.00
787.77
293.15
40000.00
783.87
298.15
40000.00
780.01
303.15
40000.00
776.1
308.15
40000.00
772.26
313.15
40000.00
768.36
318.15
40000.00
764.55
323.15
40000.00
760.68
328.15
40000.00
756.87
333.15
40000.00
753.02
283.15
45000.00
794.97
288.15
45000.00
791.13
293.15
45000.00
787.34
298.15
45000.00
783.52
303.15
45000.00
779.71
308.15
45000.00
775.95
313.15
45000.00
772.14
318.15
45000.00
768.4
323.15
45000.00
764.61
328.15
45000.00
760.88
333.15
45000.00
757.13
283.15
50000.00
798.13
288.15
50000.00
794.37
293.15
50000.00
790.66
298.15
50000.00
786.91
303.15
50000.00
783.18
308.15
50000.00
779.48
313.15
50000.00
775.74
318.15
50000.00
772.07
323.15
50000.00
768.4
328.15
50000.00
764.73
333.15
50000.00
761.02
283.15
55000.00
801.25
288.15
55000.00
797.51
293.15
55000.00
793.86
298.15
55000.00
790.19
303.15
55000.00
786.51
308.15
55000.00
782.89
313.15
55000.00
779.22
318.15
55000.00
775.65
323.15
55000.00
771.97
328.15
55000.00
768.42
333.15
55000.00
764.8
283.15
60000.00
804.23
288.15
60000.00
800.57
293.15
60000.00
796.96
298.15
60000.00
793.36
303.15
60000.00
789.75
308.15
60000.00
786.19
313.15
60000.00
782.57
318.15
60000.00
779.08
323.15
60000.00
775.47
328.15
60000.00
771.99
333.15
60000.00
768.41
283.15
65000.00
807.14
288.15
65000.00
803.54
293.15
65000.00
799.99
298.15
65000.00
796.44
303.15
65000.00
792.89
308.15
65000.00
789.36
313.15
65000.00
785.85
318.15
65000.00
782.35
323.15
65000.00
778.87
328.15
65000.00
775.41
333.15
65000.00
771.92
Reference
Correlations
Similar Compounds
Find more compounds similar to Butane, 1-ethoxy- .
Mixtures
Butane, 1-ethoxy- + Butane, 1-chloro-
Butane, 1-ethoxy- + Butane, 2-chloro-
Butane, 1-ethoxy- + Propane, 1-chloro-2-methyl-
Butane, 1-ethoxy- + Propane, 2-chloro-2-methyl-
Butane, 1-ethoxy- + Heptane
Hexane, tetradecafluoro- + Butane, 1-ethoxy-
Butane, 1-ethoxy- + Perfluorooctane
Sources
KDB Pure (Korean Thermophysical Properties Databank)
KDB Vapor Pressure Data
Crippen Method
Crippen Method
Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
Thermodynamic study of perfluorohexane + ether mixtures VLE, LLE, and HE
Experimental and modeled volumetric behavior of linear and branched ethers
Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Vapor Liquid Equilibria Measurements for Di-n-Propyl Ether and Butyl Ethyl Ether with n-Heptane
Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
Vapor-Liquid Equilibrium Data for the Binary Decafluoropentane (HFC-43-10meec) + Heptane, Decafluoropentane + Butyl Ethyl Ether, Octafluorobutane (HFC-338pcc) + Butyl Ethyl Ether, and Heptafluoro Propyl Methyl Ether (HFE-347mcc) + HFC-338pcc Systems at 101.3 kPa
Density, Viscosity, and Thermal Conductivity of Mixtures of 1-Ethoxy-1,1,2,2,3,3,4,4,4-nonafluorobutane (HFE 7200) with Methanol and 1-Ethoxybutane
Joback Method
KDB
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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