Property
Value
Unit
Temperature (K)
Source
Cp,gas
[160.65; 233.21]
J/mol×K
[374.58; 569.89]
Cp,gas
160.65
J/mol×K
374.58
Joback Calculated Property
Cp,gas
174.11
J/mol×K
407.13
Joback Calculated Property
Cp,gas
187.01
J/mol×K
439.68
Joback Calculated Property
Cp,gas
199.37
J/mol×K
472.23
Joback Calculated Property
Cp,gas
211.18
J/mol×K
504.79
Joback Calculated Property
Cp,gas
222.45
J/mol×K
537.34
Joback Calculated Property
Cp,gas
233.21
J/mol×K
569.89
Joback Calculated Property
η
[0.0002703; 0.0028144]
Pa×s
[190.51; 374.58]
η
0.0028144
Pa×s
190.51
Joback Calculated Property
η
0.0014527
Pa×s
221.19
Joback Calculated Property
η
0.0008809
Pa×s
251.87
Joback Calculated Property
η
0.0005954
Pa×s
282.54
Joback Calculated Property
η
0.0004346
Pa×s
313.22
Joback Calculated Property
η
0.0003355
Pa×s
343.90
Joback Calculated Property
η
0.0002703
Pa×s
374.58
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