Contents
Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[230.19; 282.03]
J/mol×K
[451.28; 612.56]
Cp,gas
230.19
J/mol×K
451.28
Joback Calculated Property
Cp,gas
239.54
J/mol×K
478.16
Joback Calculated Property
Cp,gas
248.61
J/mol×K
505.04
Joback Calculated Property
Cp,gas
257.39
J/mol×K
531.92
Joback Calculated Property
Cp,gas
265.89
J/mol×K
558.80
Joback Calculated Property
Cp,gas
274.10
J/mol×K
585.68
Joback Calculated Property
Cp,gas
282.03
J/mol×K
612.56
Joback Calculated Property
Cp,liquid
[261.70; 293.60]
J/mol×K
[275.15; 339.15]
Cp,liquid
261.70
J/mol×K
275.15
Measure...
Cp,liquid
262.60
J/mol×K
277.15
Measure...
Cp,liquid
263.60
J/mol×K
279.15
Measure...
Cp,liquid
264.60
J/mol×K
281.15
Measure...
Cp,liquid
265.60
J/mol×K
283.15
Measure...
Cp,liquid
266.60
J/mol×K
285.15
Measure...
Cp,liquid
267.60
J/mol×K
287.15
Measure...
Cp,liquid
268.50
J/mol×K
289.15
Measure...
Cp,liquid
269.50
J/mol×K
291.15
Measure...
Cp,liquid
270.50
J/mol×K
293.15
Measure...
Cp,liquid
271.50
J/mol×K
295.15
Measure...
Cp,liquid
272.50
J/mol×K
297.15
Measure...
Cp,liquid
273.00
J/mol×K
298.15
Measure...
Cp,liquid
273.10
J/mol×K
298.15
NIST
Cp,liquid
270.60
J/mol×K
298.15
NIST
Cp,liquid
273.30
J/mol×K
298.15
NIST
Cp,liquid
273.50
J/mol×K
299.15
Measure...
Cp,liquid
274.50
J/mol×K
301.15
Measure...
Cp,liquid
275.50
J/mol×K
303.15
Measure...
Cp,liquid
276.50
J/mol×K
305.15
Measure...
Cp,liquid
277.50
J/mol×K
307.15
Measure...
Cp,liquid
278.50
J/mol×K
309.15
Measure...
Cp,liquid
279.50
J/mol×K
311.15
Measure...
Cp,liquid
280.50
J/mol×K
313.15
Measure...
Cp,liquid
281.50
J/mol×K
315.15
Measure...
Cp,liquid
282.50
J/mol×K
317.15
Measure...
Cp,liquid
283.50
J/mol×K
319.15
Measure...
Cp,liquid
284.50
J/mol×K
321.15
Measure...
Cp,liquid
285.50
J/mol×K
323.15
Measure...
Cp,liquid
286.50
J/mol×K
325.15
Measure...
Cp,liquid
287.50
J/mol×K
327.15
Measure...
Cp,liquid
288.50
J/mol×K
329.15
Measure...
Cp,liquid
289.60
J/mol×K
331.15
Measure...
Cp,liquid
290.60
J/mol×K
333.15
Measure...
Cp,liquid
291.60
J/mol×K
335.15
Measure...
Cp,liquid
292.60
J/mol×K
337.15
Measure...
Cp,liquid
293.60
J/mol×K
339.15
Measure...
η
[0.0019459; 0.0027820]
Pa×s
[298.15; 313.15]
η
0.0027820
Pa×s
298.15
Densiti...
η
0.0027817
Pa×s
298.15
Conduct...
η
0.0024993
Pa×s
303.15
Conduct...
η
0.0022060
Pa×s
308.15
Densiti...
η
0.0022064
Pa×s
308.15
Conduct...
η
0.0019459
Pa×s
313.15
Conduct...
Δfus H
11.80
kJ/mol
199.50
NIST
Δvap H
[49.50; 52.60]
kJ/mol
[372.50; 389.50]
Δvap H
51.20
kJ/mol
372.50
NIST
Δvap H
49.50
kJ/mol
389.50
NIST
Δvap H
52.60
kJ/mol
389.50
NIST
Pvap
[28.10; 95.30]
kPa
[406.80; 442.49]
Pvap
28.10
kPa
406.80
Vapor-l...
Pvap
34.20
kPa
412.10
Vapor-l...
Pvap
41.30
kPa
417.35
Vapor-l...
Pvap
47.90
kPa
421.57
Vapor-l...
Pvap
53.70
kPa
424.90
Vapor-l...
Pvap
60.50
kPa
428.43
Vapor-l...
Pvap
68.60
kPa
432.22
Vapor-l...
Pvap
76.40
kPa
435.52
Vapor-l...
Pvap
81.20
kPa
437.42
Vapor-l...
Pvap
88.70
kPa
440.20
Vapor-l...
Pvap
93.90
kPa
441.30
Estimat...
Pvap
93.60
kPa
441.50
Estimat...
Pvap
94.10
kPa
442.10
Estimat...
Pvap
95.30
kPa
442.49
Vapor-l...
n 0
[1.40701; 1.42260]
[283.15; 323.15]
n 0
1.42260
283.15
Density...
n 0
1.41960
293.15
Density...
n 0
1.41710
298.15
Density...
n 0
1.41570
303.15
Density...
n 0
1.41500
303.15
Densiti...
n 0
1.41139
313.15
Density...
n 0
1.40701
323.15
Density...
ρl
[848.30; 900.64]
kg/m3
[293.15; 353.15]
ρl
900.64
kg/m3
293.15
Liquid ...
ρl
900.40
kg/m3
293.15
Density...
ρl
896.16
kg/m3
298.15
Experim...
ρl
896.20
kg/m3
298.15
Density...
ρl
896.17
kg/m3
298.15
Thermod...
ρl
896.25
kg/m3
298.15
Excess ...
ρl
896.31
kg/m3
298.15
Thermod...
ρl
896.46
kg/m3
298.15
FT-IR s...
ρl
896.31
kg/m3
298.15
Thermod...
ρl
896.16
kg/m3
298.15
Electri...
ρl
892.22
kg/m3
303.15
FT-IR s...
ρl
892.00
kg/m3
303.15
Density...
ρl
887.80
kg/m3
308.15
Density...
ρl
887.97
kg/m3
308.15
FT-IR s...
ρl
883.80
kg/m3
313.15
Liquid ...
ρl
883.50
kg/m3
313.15
Density...
ρl
883.70
kg/m3
313.15
FT-IR s...
ρl
879.42
kg/m3
318.15
FT-IR s...
ρl
879.20
kg/m3
318.15
Density...
ρl
874.90
kg/m3
323.15
Density...
ρl
870.60
kg/m3
328.15
Density...
ρl
866.20
kg/m3
333.15
Density...
ρl
861.80
kg/m3
338.15
Density...
ρl
857.30
kg/m3
343.15
Density...
ρl
852.80
kg/m3
348.15
Density...
ρl
848.30
kg/m3
353.15
Density...
csound,fluid
[1242.10; 1304.00]
m/s
[298.15; 318.15]
csound,fluid
1304.00
m/s
298.15
Densiti...
csound,fluid
1288.50
m/s
303.15
Densiti...
csound,fluid
1275.00
m/s
308.15
Densiti...
csound,fluid
1285.00
m/s
308.15
Densiti...
csound,fluid
1259.00
m/s
313.15
Densiti...
csound,fluid
1242.10
m/s
318.15
Densiti...
λ
[0.12; 0.14]
W/m×K
[283.96; 373.84]
λ
0.14
W/m×K
283.96
Thermal...
λ
0.14
W/m×K
293.67
Thermal...
λ
0.14
W/m×K
303.56
Thermal...
λ
0.13
W/m×K
314.25
Thermal...
λ
0.13
W/m×K
323.88
Thermal...
λ
0.13
W/m×K
333.98
Thermal...
λ
0.13
W/m×K
344.05
Thermal...
λ
0.13
W/m×K
354.63
Thermal...
λ
0.13
W/m×K
363.59
Thermal...
λ
0.12
W/m×K
373.84
Thermal...
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
444.20
K
99.10
NIST
Datasets
Mass density, kg/m3 (1)
Thermal conductivity, W/m/K (1)
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
283.15
100.00
907.9
283.15
1000.00
908.3
283.15
3000.00
909.9
283.15
5000.00
911.0
283.15
10000.00
914.2
283.15
15000.00
917.1
283.15
20000.00
920.0
283.15
25000.00
922.8
283.15
30000.00
925.6
283.15
35000.00
928.4
283.15
40000.00
930.9
283.15
50000.00
935.7
283.15
60000.00
940.5
293.15
100.00
900.5
293.15
1000.00
900.6
293.15
3000.00
902.2
293.15
5000.00
903.2
293.15
10000.00
906.8
293.15
15000.00
910.0
293.15
20000.00
912.9
293.15
25000.00
915.9
293.15
30000.00
918.8
293.15
35000.00
921.4
293.15
40000.00
924.0
293.15
50000.00
929.5
293.15
60000.00
933.9
303.15
100.00
891.8
303.15
1000.00
892.1
303.15
3000.00
893.9
303.15
5000.00
895.4
303.15
10000.00
898.9
303.15
15000.00
902.0
303.15
20000.00
905.5
303.15
25000.00
908.7
303.15
30000.00
911.8
303.15
35000.00
914.5
303.15
40000.00
916.7
303.15
50000.00
921.8
303.15
60000.00
927.1
313.15
100.00
883.5
313.15
1000.00
884.0
313.15
3000.00
885.6
313.15
5000.00
887.1
313.15
10000.00
890.7
313.15
15000.00
894.1
313.15
20000.00
897.3
313.15
25000.00
900.7
313.15
30000.00
903.6
313.15
35000.00
906.7
313.15
40000.00
909.4
313.15
50000.00
915.1
313.15
60000.00
920.1
323.15
100.00
874.0
323.15
1000.00
875.0
323.15
3000.00
876.5
323.15
5000.00
878.1
323.15
10000.00
881.9
323.15
15000.00
885.5
323.15
20000.00
889.1
323.15
25000.00
892.1
323.15
30000.00
895.4
323.15
35000.00
898.5
323.15
40000.00
901.6
323.15
50000.00
907.3
323.15
60000.00
912.9
333.15
100.00
865.6
333.15
1000.00
866.1
333.15
3000.00
868.0
333.15
5000.00
869.5
333.15
10000.00
873.5
333.15
15000.00
877.3
333.15
20000.00
880.9
333.15
25000.00
884.4
333.15
30000.00
887.6
333.15
35000.00
890.8
333.15
40000.00
894.0
333.15
50000.00
900.1
333.15
60000.00
905.7
343.15
100.00
856.5
343.15
1000.00
857.4
343.15
3000.00
859.3
343.15
5000.00
861.1
343.15
10000.00
865.1
343.15
15000.00
869.1
343.15
20000.00
873.2
343.15
25000.00
876.5
343.15
30000.00
880.1
343.15
35000.00
883.5
343.15
40000.00
886.7
343.15
50000.00
893.0
343.15
60000.00
898.6
353.15
100.00
847.5
353.15
1000.00
848.4
353.15
3000.00
850.5
353.15
5000.00
852.2
353.15
10000.00
856.7
353.15
15000.00
860.9
353.15
20000.00
864.8
353.15
25000.00
868.7
353.15
30000.00
872.3
353.15
35000.00
875.9
353.15
40000.00
879.2
353.15
50000.00
885.6
353.15
60000.00
891.8
363.15
100.00
838.2
363.15
1000.00
839.4
363.15
3000.00
841.4
363.15
5000.00
843.4
363.15
10000.00
847.9
363.15
15000.00
852.6
363.15
20000.00
856.4
363.15
25000.00
860.4
363.15
30000.00
864.4
363.15
35000.00
868.1
363.15
40000.00
871.8
363.15
50000.00
878.4
363.15
60000.00
884.8
Reference
Thermal conductivity, W/m/K
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Thermal conductivity, W/m/K - Liquid
304.15
100.00
0.1529
304.15
16400.00
0.1579
304.15
27300.00
0.1612
304.15
41800.00
0.1646
304.15
56100.00
0.1689
304.15
70200.00
0.1722
304.15
79000.00
0.1740
304.15
83500.00
0.1749
304.15
98200.00
0.1785
304.15
112200.00
0.1820
304.15
124100.00
0.1836
304.15
140100.00
0.1870
304.15
149200.00
0.1885
304.15
100.00
0.1533
321.15
100.00
0.1497
321.15
16400.00
0.1548
321.15
27300.00
0.1585
321.15
41800.00
0.1628
321.15
56100.00
0.1665
321.15
70200.00
0.1701
321.15
84200.00
0.1739
321.15
98200.00
0.1770
321.15
112200.00
0.1800
321.15
126200.00
0.1830
321.15
134900.00
0.1851
321.15
150600.00
0.1879
321.15
100.00
0.1496
338.15
100.00
0.1461
338.15
16400.00
0.1518
338.15
27300.00
0.1555
338.15
41800.00
0.1601
338.15
56100.00
0.1640
338.15
70200.00
0.1677
338.15
84200.00
0.1717
338.15
98200.00
0.1751
338.15
108700.00
0.1775
338.15
123400.00
0.1807
338.15
140100.00
0.1844
338.15
100.00
0.1463
Reference
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.65]
kPa
[341.68; 468.10]
The Yaw...
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.63176e+01 Coefficient B -4.43972e+03 Coefficient C -6.47130e+01 Temperature range, min. 341.68
Temperature range, max. 468.10
Pvap
1.33
kPa
341.68
Calculated Property
Pvap
2.89
kPa
355.73
Calculated Property
Pvap
5.84
kPa
369.77
Calculated Property
Pvap
11.07
kPa
383.82
Calculated Property
Pvap
19.91
kPa
397.87
Calculated Property
Pvap
34.14
kPa
411.91
Calculated Property
Pvap
56.13
kPa
425.96
Calculated Property
Pvap
88.91
kPa
440.01
Calculated Property
Pvap
136.24
kPa
454.05
Calculated Property
Pvap
202.65
kPa
468.10
Calculated Property
Similar Compounds
Find more compounds similar to Ethanol, 2-butoxy- .
Mixtures
Ethanol, 2-butoxy- + 1-Butanol, 3-methyl-
Ethanol, 2-butoxy- + 2-Pyrrolidinone, 1-methyl-
1-Propanol + Ethanol, 2-butoxy-
Ethanol, 2-butoxy- + Isopropyl Alcohol
Ethanol, 2-butoxy- + 1-Butanol
Ethanol, 2-butoxy- + Octane + Water
n-Hexane + Ethanol, 2-butoxy-
Ethanol, 2-butoxy- + Heptane
Ethanol, 2-butoxy- + 1-Hexanol
Ethanol, 2-butoxy- + 1-Octanol
Ethanol, 2-butoxy- + 1-Decanol
Ethanol, 2-butoxy- + Water
Ethanol, 2-butoxy- + Benzyl alcohol
Ethanol, 2-butoxy- + Methyl Alcohol
Ethanol, 2-butoxy- + Ethanol
Ethanol, 2-butoxy- + Propanoic acid, 2-hydroxy-, ethyl ester
Ethanol, 2-butoxy- + Phosphonic acid, phenyl-
Ethanol, 2-butoxy- + Ethanol, 2-(methylamino)-
Benzene + Ethanol, 2-butoxy-
Toluene + Ethanol, 2-butoxy-
Find more mixtures with Ethanol, 2-butoxy- .
Sources
Crippen Method
Densities, Viscosities, Sound Speeds, Refractive Indices, and Excess Properties of Binary Mixtures of Isoamyl Alcohol with Some Alkoxyethanols
Vapor-liquid equilibria and excess molar volumes of N-methyl-2-pyrrolidone with 2-alkoxyethanols
Thermodynamic and spectral investigations of binary liquid mixturesof 2-butoxy ethanol with alcohols at temperature range of 293.15-313.15 K
Liquid liquid equilibria for the ternary system water + octane + 2-butyloxy-ethanol
Phase behavior of glycol ether surfactant systems in the presence of brine and hydrocarbon: Experiment and modeling
Solubility of disodium 4,4'-dinitrobibenzyl-2,2'-disulfonate in aqueous organic solutions and its effects on the oxidation reaction of DSD acid synthesis
Thermodynamic properties and sPC-SAFT modeling of 2-ethoxyethanol, 2-propoxyethanol and 2-butoxyethanol from T = (293.15-413.15) K and pressure up to 30 MPa
Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ethylene glycol ethers at T = 298.15 K
Phase equilibria for mixtures containing nonionic surfactant systems: Modeling and experiments
Effect of hydrophilic additives on volumetric and viscosity properties of amino acids in aqueous solutions at T = (283.15 to 333.15) K
Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
Solubility of disodium 4,4'-dinitrostilbene-2,2'-disulfonate and sodium 4-nitrotoluene-2-sulfonate in aqueous organic solutions and its application feasibility in oxidation stage of DSD acid synthesis
FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
Experimental study on the calorimetric data of 2-butoxyethanol with aliphatic alcohols (C1-C4) and correlation with the Wilson, NRTL and UNIQUAC models at T = 298 K
Densities, speed of sound, and IR studies of Ethyl lactate with 2-alkoxyethanols at different temperatures
Measurement and Prediction of Molar Heat Capacities of Liquid Polyoxyethylene Glycol Monoalkyl Ethers (CnEm)
Densities of Diethylene Glycol, Monobutyl Ether, Diethylene Glycol Dibutyl Ether, and Ethylene Glycol Monobutyl Ether from (283.15 to 363.15) K at Pressures up to 60 MPa
Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
Density, Viscosity, and Excess Properties of Binary Mixtures of 2-(Methylamino)ethanol with 2-Methoxyethanol, 2-Ethoxyethanol, and 2-Butoxyethanol from 293.15 to 353.15 K
Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
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
Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
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
Thermal Conductivity of Aqueous Mixtures of 2-n-Butoxyethanol at Pressures up to 150 MPa
Estimation of Activity Coefficients for the Pairs of the System 2-Ethoxyethanol + 2-Ethoxyethyl Acetate + 2-Butoxyethanol + 2-Butoxyethyl Acetate
Conductance Studies of Tetrabutylammonium Bromide, Sodium Bromide, and Sodium Tetraphenylborate in 2-Butoxyethanol (1) + Water (2) Mixtures at (298.15, 303.15, 308.15, and 313.15) K
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
Electrical Conductance of Some Tetraalkylammonium Bromide Salts in 2-Butoxyethanol (1) + Water (2) mixtures at (298.15, 303.15, 308.15, and 313.15) K
Density, Viscosity, Refractive Index, and Ultrasonic Speed of Binary Mixtures of 1,3-Dioxolane with 2-Methoxyethanol, 2-Ethoxyethanol, 2-Butoxyethanol, 2-Propylamine, and Cyclohexylamine
Density, Viscosity, and Refractive Index for Water + 2-Butoxyethanol and + 2-(2-Butoxyethoxy)ethanol at Various Temperatures
Density, Speed of Sound, and Refractive Index of Aqueous Binary Mixtures of Some Glycol Ethers at T = 298.15 K
Joback Method
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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