Property
Value
Unit
Temperature (K)
Source
Cp,gas
[160.57; 233.11]
J/mol×K
[374.38; 569.58]
Cp,gas
160.57
J/mol×K
374.38
Joback Calculated Property
Cp,gas
174.02
J/mol×K
406.91
Joback Calculated Property
Cp,gas
186.92
J/mol×K
439.45
Joback Calculated Property
Cp,gas
199.27
J/mol×K
471.98
Joback Calculated Property
Cp,gas
211.08
J/mol×K
504.52
Joback Calculated Property
Cp,gas
222.36
J/mol×K
537.05
Joback Calculated Property
Cp,gas
233.11
J/mol×K
569.58
Joback Calculated Property
η
[0.0002706; 0.0028144]
Pa×s
[190.51; 374.38]
η
0.0028144
Pa×s
190.51
Joback Calculated Property
η
0.0014536
Pa×s
221.16
Joback Calculated Property
η
0.0008817
Pa×s
251.80
Joback Calculated Property
η
0.0005961
Pa×s
282.44
Joback Calculated Property
η
0.0004351
Pa×s
313.09
Joback Calculated Property
η
0.0003360
Pa×s
343.74
Joback Calculated Property
η
0.0002706
Pa×s
374.38
Joback Calculated Property
Pvap
[0.40; 7.43]
kPa
[258.55; 308.25]
Pvap
0.40
kPa
258.55
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
0.79
kPa
268.45
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
1.10
kPa
273.45
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
1.50
kPa
278.55
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
2.02
kPa
283.45
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
2.68
kPa
288.35
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
3.52
kPa
293.35
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
4.57
kPa
298.35
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
5.88
kPa
303.35
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap
7.43
kPa
308.25
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
n 0
[1.41820; 1.41992]
[298.00; 298.15]
n 0
1.41833
298.00
Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
n 0
1.41820
298.15
Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
n 0
1.41992
298.15
Experimental Determination of Isobaric Vapor-Liquid Equilibrium and Isothermal Interfacial Tensions for the Binary Ethanol + Cyclopentyl Methyl Ether Mixture
ρl
[860.13; 860.43]
kg/m3
[293.15; 293.15]
ρl
860.13
kg/m3
293.15
Liquid-Liquid Phase Equilibria for Quinary, Quaternary, and Ternary Systems {Water + Furfural + Acetic Acid + Cyclopentyl Methyl Ether + CaCl2}: Measurement, Effect of Salt ,and Comparative Study
ρl
860.43
kg/m3
293.15
Measurements and Comparative Study of Ternary Liquid Liquid Equilibria for Water + Acrylic Acid + Cyclopentyl Methyl Ether at (293.15, 303.15, and 313.15) K and 100.249 kPa