| Property |
Value |
Unit |
Temperature (K) |
Source |
| Cp,gas |
[138.07; 206.30] |
J/mol×K |
[370.00; 544.00] |
|
|
|
| Cp,gas |
138.07 |
J/mol×K |
370.00 |
NIST
|
| Cp,gas |
143.10 ± 1.30 |
J/mol×K |
384.00 |
NIST
|
| Cp,gas |
146.44 |
J/mol×K |
390.00 |
NIST
|
| Cp,gas |
153.97 |
J/mol×K |
410.00 |
NIST
|
| Cp,gas |
161.80 ± 1.70 |
J/mol×K |
428.00 |
NIST
|
| Cp,gas |
174.50 ± 1.70 |
J/mol×K |
460.00 |
NIST
|
| Cp,gas |
189.50 ± 2.10 |
J/mol×K |
495.00 |
NIST
|
| Cp,gas |
196.70 ± 2.10 |
J/mol×K |
521.00 |
NIST
|
| Cp,gas |
206.30 ± 2.10 |
J/mol×K |
544.00 |
NIST
|
| Cp,liquid |
[100.40; 311.00] |
J/mol×K |
[280.00; 520.00] |
|
|
|
| Cp,liquid |
149.30 |
J/mol×K |
280.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
153.10 |
J/mol×K |
290.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
155.13 |
J/mol×K |
293.15 |
NIST
|
| Cp,liquid |
154.80 |
J/mol×K |
293.15 |
NIST
|
| Cp,liquid |
153.75 |
J/mol×K |
293.15 |
Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
|
| Cp,liquid |
154.81 |
J/mol×K |
293.15 |
NIST
|
| Cp,liquid |
155.85 |
J/mol×K |
295.00 |
NIST
|
| Cp,liquid |
176.10 |
J/mol×K |
298.00 |
NIST
|
| Cp,liquid |
155.31 |
J/mol×K |
298.00 |
NIST
|
| Cp,liquid |
152.93 |
J/mol×K |
298.00 |
NIST
|
| Cp,liquid |
155.50 |
J/mol×K |
298.00 |
NIST
|
| Cp,liquid |
156.70 |
J/mol×K |
298.00 |
NIST
|
| Cp,liquid |
156.07 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.20 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.20 |
J/mol×K |
298.15 |
Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
|
| Cp,liquid |
156.31 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.20 |
J/mol×K |
298.15 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
155.20 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
159.60 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.07 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.12 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.35 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.40 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.12 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.15 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.00 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.40 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
155.96 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.50 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.00 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
156.90 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
155.85 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
155.96 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
154.32 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
157.06 |
J/mol×K |
298.15 |
NIST
|
| Cp,liquid |
143.90 |
J/mol×K |
298.90 |
NIST
|
| Cp,liquid |
156.90 |
J/mol×K |
300.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
154.20 |
J/mol×K |
300.00 |
NIST
|
| Cp,liquid |
158.95 |
J/mol×K |
303.15 |
Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
|
| Cp,liquid |
100.40 |
J/mol×K |
304.20 |
NIST
|
| Cp,liquid |
160.80 |
J/mol×K |
310.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
155.20 |
J/mol×K |
311.00 |
NIST
|
| Cp,liquid |
164.70 |
J/mol×K |
320.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
143.90 |
J/mol×K |
326.50 |
NIST
|
| Cp,liquid |
168.70 |
J/mol×K |
330.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
172.90 |
J/mol×K |
340.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
177.30 |
J/mol×K |
350.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
181.90 |
J/mol×K |
360.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
186.90 |
J/mol×K |
370.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
192.00 |
J/mol×K |
380.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
197.40 |
J/mol×K |
390.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
202.80 |
J/mol×K |
400.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
208.10 |
J/mol×K |
410.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
213.40 |
J/mol×K |
420.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
218.50 |
J/mol×K |
430.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
223.40 |
J/mol×K |
440.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
228.00 |
J/mol×K |
450.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
233.00 |
J/mol×K |
460.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
239.00 |
J/mol×K |
470.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
247.00 |
J/mol×K |
480.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
258.00 |
J/mol×K |
490.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
271.00 |
J/mol×K |
500.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
289.00 |
J/mol×K |
510.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| Cp,liquid |
311.00 |
J/mol×K |
520.00 |
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
|
| η |
[0.0005195; 0.0011802] |
Pa×s |
[283.15; 333.15] |
|
|
|
| η |
0.0011802 |
Pa×s |
283.15 |
Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
|
| η |
0.0010770 |
Pa×s |
288.15 |
Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
|
| η |
0.0009840 |
Pa×s |
293.15 |
Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
|
| η |
0.0009847 |
Pa×s |
293.15 |
Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
|
| η |
0.0009840 |
Pa×s |
293.15 |
Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
|
| η |
0.0009680 |
Pa×s |
293.15 |
Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
|
| η |
0.0009680 |
Pa×s |
293.15 |
Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
|
| η |
0.0009680 |
Pa×s |
293.15 |
Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
|
| η |
0.0009027 |
Pa×s |
298.15 |
Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
|
| η |
0.0009030 |
Pa×s |
298.15 |
Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
|
| η |
0.0009030 |
Pa×s |
298.15 |
Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
|
| η |
0.0008980 |
Pa×s |
298.15 |
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
|
| η |
0.0008870 |
Pa×s |
298.15 |
Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
|
| η |
0.0008945 |
Pa×s |
298.15 |
Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
|
| η |
0.0008870 |
Pa×s |
298.15 |
Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
|
| η |
0.0008870 |
Pa×s |
298.15 |
Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
|
| η |
0.0009040 |
Pa×s |
298.15 |
Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
|
| η |
0.0008230 |
Pa×s |
303.15 |
Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
|
| η |
0.0008160 |
Pa×s |
303.15 |
Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
|
| η |
0.0008295 |
Pa×s |
303.15 |
Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
|
| η |
0.0008205 |
Pa×s |
303.15 |
Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
|
| η |
0.0008090 |
Pa×s |
303.15 |
Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
|
| η |
0.0008300 |
Pa×s |
303.15 |
Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
|
| η |
0.0008160 |
Pa×s |
303.15 |
Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
|
| η |
0.0008300 |
Pa×s |
303.15 |
Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
|
| η |
0.0008284 |
Pa×s |
303.15 |
Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
|
| η |
0.0008160 |
Pa×s |
303.15 |
Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
|
| η |
0.0008210 |
Pa×s |
303.15 |
Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
|
| η |
0.0007720 |
Pa×s |
308.15 |
Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
|
| η |
0.0007490 |
Pa×s |
308.15 |
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
|
| η |
0.0007637 |
Pa×s |
308.15 |
Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
|
| η |
0.0007640 |
Pa×s |
308.15 |
Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
|
| η |
0.0006980 |
Pa×s |
313.15 |
Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
|
| η |
0.0007061 |
Pa×s |
313.15 |
Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
|
| η |
0.0006963 |
Pa×s |
313.15 |
Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
|
| η |
0.0006850 |
Pa×s |
313.15 |
Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
|
| η |
0.0006960 |
Pa×s |
313.15 |
Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
|
| η |
0.0006040 |
Pa×s |
323.15 |
Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
|
| η |
0.0005978 |
Pa×s |
323.15 |
Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
|
| η |
0.0005984 |
Pa×s |
323.15 |
Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
|
| η |
0.0005980 |
Pa×s |
323.15 |
Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
|
| η |
0.0005195 |
Pa×s |
333.15 |
Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
|
| η |
0.0005200 |
Pa×s |
333.15 |
Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
|
| ΔfusH |
[2.68; 6.74] |
kJ/mol |
[186.10; 279.80] |
|
| ΔfusH |
6.74 |
kJ/mol |
186.10 |
NIST
|
| ΔfusH |
2.68 |
kJ/mol |
279.80 |
NIST
|
| ΔfusH |
2.68 |
kJ/mol |
279.80 |
NIST
|
| ΔsubH |
[27.60; 46.60] |
kJ/mol |
[186.00; 274.00] |
|
|
|
| ΔsubH |
46.60 |
kJ/mol |
186.00 |
NIST
|
| ΔsubH |
37.70 |
kJ/mol |
248.00 |
NIST
|
| ΔsubH |
27.60 |
kJ/mol |
251.50 |
NIST
|
| ΔsubH |
37.20 |
kJ/mol |
273.00 |
NIST
|
| ΔsubH |
36.50 |
kJ/mol |
274.00 |
NIST
|
| ΔvapH |
[29.60; 33.33] |
kJ/mol |
[298.00; 521.00] |
|
|
|
| ΔvapH |
32.83 |
kJ/mol |
298.00 |
Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
|
| ΔvapH |
33.33 |
kJ/mol |
298.15 |
NIST
|
| ΔvapH |
32.20 ± 0.10 |
kJ/mol |
313.00 |
NIST
|
| ΔvapH |
32.30 ± 0.10 |
kJ/mol |
313.00 |
NIST
|
| ΔvapH |
32.30 |
kJ/mol |
314.00 |
NIST
|
| ΔvapH |
32.70 |
kJ/mol |
322.50 |
NIST
|
| ΔvapH |
32.90 |
kJ/mol |
323.00 |
NIST
|
| ΔvapH |
32.50 |
kJ/mol |
323.00 |
NIST
|
| ΔvapH |
31.90 ± 0.10 |
kJ/mol |
323.00 |
NIST
|
| ΔvapH |
32.90 |
kJ/mol |
324.00 |
NIST
|
| ΔvapH |
31.40 ± 0.10 |
kJ/mol |
324.00 |
NIST
|
| ΔvapH |
31.90 |
kJ/mol |
324.50 |
NIST
|
| ΔvapH |
33.10 |
kJ/mol |
324.50 |
NIST
|
| ΔvapH |
31.10 |
kJ/mol |
332.00 |
NIST
|
| ΔvapH |
31.10 ± 0.10 |
kJ/mol |
333.00 |
NIST
|
| ΔvapH |
31.20 ± 0.10 |
kJ/mol |
333.00 |
NIST
|
| ΔvapH |
32.80 |
kJ/mol |
335.00 |
NIST
|
| ΔvapH |
31.00 ± 0.10 |
kJ/mol |
338.00 |
NIST
|
| ΔvapH |
30.60 ± 0.10 |
kJ/mol |
343.00 |
NIST
|
| ΔvapH |
30.30 |
kJ/mol |
345.00 |
NIST
|
| ΔvapH |
30.40 ± 0.10 |
kJ/mol |
346.00 |
NIST
|
| ΔvapH |
30.40 ± 0.10 |
kJ/mol |
348.00 |
NIST
|
| ΔvapH |
30.10 ± 0.10 |
kJ/mol |
353.00 |
NIST
|
| ΔvapH |
29.96 |
kJ/mol |
353.90 |
KDB
|
| ΔvapH |
29.97 |
kJ/mol |
353.90 |
NIST
|
| ΔvapH |
30.10 ± 0.10 |
kJ/mol |
354.00 |
NIST
|
| ΔvapH |
30.10 |
kJ/mol |
354.00 |
NIST
|
| ΔvapH |
30.00 |
kJ/mol |
355.00 |
NIST
|
| ΔvapH |
30.90 |
kJ/mol |
383.50 |
NIST
|
| ΔvapH |
32.20 |
kJ/mol |
415.00 |
NIST
|
| ΔvapH |
29.60 |
kJ/mol |
451.50 |
NIST
|
| ΔvapH |
29.60 |
kJ/mol |
521.00 |
NIST
|
| Pvap |
[2.08; 362.80] |
kPa |
[263.15; 403.15] |
|
|
|
| Pvap |
2.08 |
kPa |
263.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
3.73 |
kPa |
273.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
3.73 |
kPa |
273.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
3.73 |
kPa |
273.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
6.36 |
kPa |
283.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
6.35 |
kPa |
283.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
6.35 |
kPa |
283.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
6.39 |
kPa |
283.32 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
6.39 |
kPa |
283.32 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
8.20 |
kPa |
288.28 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
8.20 |
kPa |
288.28 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
10.36 |
kPa |
293.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
10.36 |
kPa |
293.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
10.37 |
kPa |
293.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
10.42 |
kPa |
293.27 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
10.42 |
kPa |
293.27 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
11.15 |
kPa |
295.42 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
11.16 |
kPa |
295.45 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
11.17 |
kPa |
295.46 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
11.33 |
kPa |
295.72 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
11.35 |
kPa |
295.75 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
11.63 |
kPa |
296.22 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
12.15 |
kPa |
297.08 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
12.16 |
kPa |
297.13 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
12.17 |
kPa |
297.13 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
12.61 |
kPa |
297.86 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
12.71 |
kPa |
297.99 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
13.04 |
kPa |
298.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
13.04 |
kPa |
298.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
13.17 |
kPa |
298.25 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
13.17 |
kPa |
298.25 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
13.23 |
kPa |
298.83 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
13.80 |
kPa |
299.75 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
13.81 |
kPa |
299.77 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
14.52 |
kPa |
300.85 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
15.71 |
kPa |
302.63 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
16.06 |
kPa |
302.92 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
16.03 |
kPa |
303.02 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
16.40 |
kPa |
303.15 |
Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
|
| Pvap |
16.26 |
kPa |
303.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
16.26 |
kPa |
303.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
16.11 |
kPa |
303.15 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
16.26 |
kPa |
303.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
16.45 |
kPa |
303.27 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
16.45 |
kPa |
303.27 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
16.95 |
kPa |
304.19 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
17.04 |
kPa |
304.38 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
17.05 |
kPa |
304.40 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
17.07 |
kPa |
304.42 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
18.33 |
kPa |
306.05 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
18.60 |
kPa |
306.40 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
19.05 |
kPa |
306.91 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
19.40 |
kPa |
307.45 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
19.91 |
kPa |
308.06 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
20.00 |
kPa |
308.07 |
Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
|
| Pvap |
19.80 |
kPa |
308.15 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
20.16 |
kPa |
308.27 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
21.12 |
kPa |
309.50 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
21.56 |
kPa |
309.90 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
22.47 |
kPa |
310.98 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
23.89 |
kPa |
312.48 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
24.63 |
kPa |
313.15 |
Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
|
| Pvap |
24.56 |
kPa |
313.15 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
24.65 |
kPa |
313.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
24.65 |
kPa |
313.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
24.62 |
kPa |
313.15 |
Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
|
| Pvap |
24.70 |
kPa |
313.15 |
Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
|
| Pvap |
24.65 |
kPa |
313.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
24.61 |
kPa |
313.16 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
24.97 |
kPa |
313.24 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
24.97 |
kPa |
313.24 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
24.95 |
kPa |
313.40 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
25.25 |
kPa |
313.84 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
26.47 |
kPa |
315.01 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
26.67 |
kPa |
315.26 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
27.43 |
kPa |
315.76 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
27.88 |
kPa |
316.32 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
29.23 |
kPa |
317.51 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
29.77 |
kPa |
317.95 |
Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
|
| Pvap |
29.95 |
kPa |
318.05 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
30.03 |
kPa |
318.19 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
29.70 |
kPa |
318.30 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
30.09 |
kPa |
318.31 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
30.56 |
kPa |
318.67 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
31.93 |
kPa |
319.81 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
32.46 |
kPa |
320.11 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
33.27 |
kPa |
320.87 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
34.59 |
kPa |
321.91 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
34.69 |
kPa |
321.99 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
34.90 |
kPa |
322.06 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
35.95 |
kPa |
322.94 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
36.23 |
kPa |
323.14 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
36.27 |
kPa |
323.15 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
36.24 |
kPa |
323.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
36.24 |
kPa |
323.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
36.40 |
kPa |
323.15 |
Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
|
| Pvap |
36.24 |
kPa |
323.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
36.72 |
kPa |
323.21 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
36.72 |
kPa |
323.21 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
36.59 |
kPa |
323.44 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
37.23 |
kPa |
323.88 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
37.43 |
kPa |
323.92 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
37.33 |
kPa |
323.95 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
38.19 |
kPa |
324.72 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
38.28 |
kPa |
324.73 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
38.56 |
kPa |
324.83 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
40.00 |
kPa |
325.65 |
Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
|
| Pvap |
39.94 |
kPa |
325.66 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
39.70 |
kPa |
325.95 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
40.45 |
kPa |
326.12 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
41.25 |
kPa |
326.68 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
42.42 |
kPa |
327.32 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
42.68 |
kPa |
327.61 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
43.51 |
kPa |
328.16 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
43.97 |
kPa |
328.43 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
44.91 |
kPa |
328.90 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
45.40 |
kPa |
329.32 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
45.43 |
kPa |
329.35 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
46.59 |
kPa |
330.05 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
47.45 |
kPa |
330.44 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
48.07 |
kPa |
330.94 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
49.32 |
kPa |
331.68 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
49.68 |
kPa |
331.90 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
49.92 |
kPa |
331.94 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
49.89 |
kPa |
332.02 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
50.00 |
kPa |
332.08 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
49.70 |
kPa |
332.10 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
50.60 |
kPa |
332.41 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
51.87 |
kPa |
333.11 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
51.85 |
kPa |
333.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
52.00 |
kPa |
333.15 |
Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
|
| Pvap |
51.85 |
kPa |
333.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
51.92 |
kPa |
333.15 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
51.85 |
kPa |
333.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
51.90 |
kPa |
333.16 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
51.90 |
kPa |
333.17 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
52.48 |
kPa |
333.21 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
52.48 |
kPa |
333.21 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
52.43 |
kPa |
333.33 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
53.33 |
kPa |
333.77 |
Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
|
| Pvap |
53.15 |
kPa |
333.83 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
53.19 |
kPa |
333.86 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
53.30 |
kPa |
333.96 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
54.47 |
kPa |
334.53 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
54.76 |
kPa |
334.60 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
55.85 |
kPa |
335.26 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
56.56 |
kPa |
335.64 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
57.19 |
kPa |
335.95 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
57.44 |
kPa |
335.99 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
58.63 |
kPa |
336.70 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
58.85 |
kPa |
336.85 |
Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
|
| Pvap |
59.98 |
kPa |
337.31 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
59.96 |
kPa |
337.36 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
59.70 |
kPa |
337.45 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
60.49 |
kPa |
337.59 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
61.39 |
kPa |
338.06 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
61.40 |
kPa |
338.06 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
61.50 |
kPa |
338.15 |
Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
|
| Pvap |
61.56 |
kPa |
338.16 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
62.44 |
kPa |
338.50 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
62.63 |
kPa |
338.65 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
62.64 |
kPa |
338.67 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
63.95 |
kPa |
339.29 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
64.86 |
kPa |
339.65 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
65.29 |
kPa |
339.92 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
66.66 |
kPa |
340.43 |
Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
|
| Pvap |
66.63 |
kPa |
340.54 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
67.47 |
kPa |
340.81 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
67.95 |
kPa |
341.12 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
69.29 |
kPa |
341.72 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
69.94 |
kPa |
341.92 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
69.95 |
kPa |
341.96 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
69.80 |
kPa |
342.05 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
70.65 |
kPa |
342.32 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
71.93 |
kPa |
342.88 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
72.45 |
kPa |
342.99 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
72.39 |
kPa |
343.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
72.60 |
kPa |
343.15 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
72.39 |
kPa |
343.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
72.50 |
kPa |
343.15 |
Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
|
| Pvap |
72.40 |
kPa |
343.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
72.53 |
kPa |
343.16 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
72.98 |
kPa |
343.18 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
72.98 |
kPa |
343.18 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
73.25 |
kPa |
343.43 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
74.01 |
kPa |
343.68 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
74.73 |
kPa |
344.05 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
74.96 |
kPa |
344.05 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
75.07 |
kPa |
344.09 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
75.96 |
kPa |
344.55 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
77.27 |
kPa |
345.08 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
77.54 |
kPa |
345.11 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
77.94 |
kPa |
345.42 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
78.76 |
kPa |
345.69 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
79.92 |
kPa |
346.07 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
79.99 |
kPa |
346.11 |
Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
|
| Pvap |
80.00 |
kPa |
346.13 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
80.00 |
kPa |
346.18 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
79.90 |
kPa |
346.25 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
81.20 |
kPa |
346.58 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
81.25 |
kPa |
346.67 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
82.52 |
kPa |
347.06 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
82.56 |
kPa |
347.18 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
82.57 |
kPa |
347.18 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
83.89 |
kPa |
347.69 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
85.03 |
kPa |
348.01 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
84.73 |
kPa |
348.05 |
Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
|
| Pvap |
84.70 |
kPa |
348.15 |
Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
|
| Pvap |
85.23 |
kPa |
348.19 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
86.49 |
kPa |
348.65 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
87.27 |
kPa |
348.86 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
87.65 |
kPa |
349.15 |
Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
|
| Pvap |
87.93 |
kPa |
349.19 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
89.43 |
kPa |
349.72 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
89.99 |
kPa |
349.84 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
90.05 |
kPa |
350.00 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
90.64 |
kPa |
350.18 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
90.87 |
kPa |
350.25 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
92.07 |
kPa |
350.67 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
92.48 |
kPa |
350.73 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
93.27 |
kPa |
351.10 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
93.32 |
kPa |
351.12 |
Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
|
| Pvap |
94.84 |
kPa |
351.55 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
94.63 |
kPa |
351.57 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
95.17 |
kPa |
351.72 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
95.92 |
kPa |
352.01 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
97.23 |
kPa |
352.45 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
98.57 |
kPa |
352.90 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
99.11 |
kPa |
353.14 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
99.11 |
kPa |
353.14 |
Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
|
| Pvap |
98.87 |
kPa |
353.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
98.87 |
kPa |
353.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
98.85 |
kPa |
353.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
99.31 |
kPa |
353.15 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
99.95 |
kPa |
353.36 |
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
|
| Pvap |
101.30 |
kPa |
353.70 |
Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
|
| Pvap |
101.30 |
kPa |
353.73 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
101.33 |
kPa |
353.73 |
Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
|
| Pvap |
101.30 |
kPa |
353.82 |
A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
|
| Pvap |
101.30 |
kPa |
353.82 |
A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
|
| Pvap |
101.33 |
kPa |
353.85 |
Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
|
| Pvap |
101.30 |
kPa |
353.94 |
Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
|
| Pvap |
101.75 |
kPa |
354.05 |
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
|
| Pvap |
102.34 |
kPa |
354.11 |
Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
|
| Pvap |
132.35 |
kPa |
363.15 |
Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
|
| Pvap |
132.35 |
kPa |
363.15 |
Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
|
| Pvap |
132.33 |
kPa |
363.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
|
| Pvap |
362.80 |
kPa |
403.15 |
Isothermal Vapor-Liquid Equilibrium for Methanol and 2,3-Dimethyl-1-butene at 343.06 K, 353.27 K, 363.19 K, and 372.90 K
|
| n0 |
[1.41220; 1.43193] |
|
[283.15; 318.20] |
|
|
|
| n0 |
1.43193 |
|
283.15 |
Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
|
| n0 |
1.42590 |
|
293.15 |
Liquid-Liquid Equilibrium of (Water + Pentane-2,4-dione + Ethyl Ethanoate) and (Water + Pentane-2,4-dione + Cyclohexane) at (298.15 and 313.15) K
|
| n0 |
1.42650 |
|
293.15 |
Vapour liquid equilibrium of carboxylic acid systems: Propionic acid + valeric acid and isobutyric acid + valeric acid
|
| n0 |
1.42660 |
|
293.15 |
Solubilities of Phosphorus-Containing Compounds in Selected Solvents
|
| n0 |
1.42350 |
|
293.15 |
Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
|
| n0 |
1.42633 |
|
293.15 |
Mixing properties of binary mixtures presenting azeotropes at several temperatures
|
| n0 |
1.42630 |
|
293.20 |
Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
|
| n0 |
1.42690 |
|
293.20 |
Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
|
| n0 |
1.42360 |
|
298.15 |
(Liquid + liquid) equilibrium data for the ternary systems (cycloalkane + ethylbenzene + 1-ethyl-3-methylimidazolium ethylsulfate) at T = 298.15 K and atmospheric pressure
|
| n0 |
1.42350 |
|
298.15 |
Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7 kPa
|
| n0 |
1.42360 |
|
298.15 |
Experimental data, correlation and prediction of the extraction of benzene from cyclic hydrocarbons using [Epy][ESO4] ionic liquid
|
| n0 |
1.42320 |
|
298.15 |
Azeotropic behaviour of (benzene + cyclohexane + chlorobenzene) ternary mixture using chlorobenzene as entrainer at 101.3 kPa
|
| n0 |
1.42508 |
|
298.15 |
Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
|
| n0 |
1.42354 |
|
298.15 |
Mixing properties of binary mixtures presenting azeotropes at several temperatures
|
| n0 |
1.42354 |
|
298.15 |
KDB
|
| n0 |
1.42403 |
|
298.15 |
(Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
|
| n0 |
1.42360 |
|
298.15 |
Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
|
| n0 |
1.42360 |
|
298.15 |
Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
|
| n0 |
1.42403 |
|
298.15 |
Liquid-Liquid Equilibria for Systems Composed by 1-Methyl-3-octylimidazolium Tetrafluoroborate Ionic Liquid, Thiophene, and n-Hexane or Cyclohexane
|
| n0 |
1.42360 |
|
298.15 |
Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
|
| n0 |
1.42350 |
|
298.15 |
Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
|
| n0 |
1.42650 |
|
298.15 |
Vapor Liquid Equilibrium for Ternary and Binary Mixtures of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa
|
| n0 |
1.42356 |
|
298.15 |
Application of [HMim][NTf2], [HMim][TfO] and [BMim][TfO] ionic liquids on the extraction of toluene from alkanes: Effect of the anion and the alkyl chain length of the cation on the LLE
|
| n0 |
1.42340 |
|
298.15 |
Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
|
| n0 |
1.42508 |
|
298.15 |
Vapor liquid equilibria and interfacial tensions for the ternary system acetone + 2,2 -oxybis[propane] + cyclohexane and its constituent binary systems
|
| n0 |
1.42350 |
|
298.15 |
Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
|
| n0 |
1.42350 |
|
298.15 |
Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
|
| n0 |
1.42360 |
|
298.15 |
Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
|
| n0 |
1.42360 |
|
298.15 |
Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
|
| n0 |
1.42378 |
|
298.15 |
Liquid liquid equilibria of lactam containing binary systems
|
| n0 |
1.42360 |
|
298.15 |
Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
|
| n0 |
1.42350 |
|
298.15 |
Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
|
| n0 |
1.42360 |
|
298.15 |
Liquid Extraction of Benzene from Its Mixtures Using 1-Ethyl-3-methylimidazolium Ethylsulfate as a Solvent
|
| n0 |
1.42350 |
|
298.15 |
Phase equilibria on four binary systems containing 3-methylthiophene
|
| n0 |
1.42360 |
|
298.15 |
Liquid Liquid Extraction of Aromatic Compounds from Cycloalkanes Using 1-Butyl-3-methylimidazolium Methylsulfate Ionic Liquid
|
| n0 |
1.42340 |
|
298.20 |
(Liquid + liquid) equilibrium data of (water + phosphoric acid + solvents) systems at T = (308.2 and 318.2) K
|
| n0 |
1.42350 |
|
298.20 |
Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
|
| n0 |
1.42073 |
|
303.15 |
Mixing properties of binary mixtures presenting azeotropes at several temperatures
|
| n0 |
1.42050 |
|
308.15 |
Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
|
| n0 |
1.41740 |
|
308.20 |
Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
|
| n0 |
1.41516 |
|
313.15 |
Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
|
| n0 |
1.41220 |
|
318.20 |
Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
|
| ρl |
[89.90; 788.30] |
kg/m3 |
[287.00; 698.50] |
|
|
|
| ρl |
788.30 |
kg/m3 |
287.00 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
783.29 |
kg/m3 |
288.15 |
Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
|
| ρl |
783.00 |
kg/m3 |
288.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
778.54 |
kg/m3 |
293.00 |
Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
|
| ρl |
779.00 |
kg/m3 |
293.00 |
KDB
|
| ρl |
778.20 |
kg/m3 |
293.10 |
Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
|
| ρl |
779.00 |
kg/m3 |
293.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
778.00 |
kg/m3 |
293.15 |
Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
|
| ρl |
778.56 |
kg/m3 |
293.15 |
Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
|
| ρl |
778.70 |
kg/m3 |
293.15 |
Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
|
| ρl |
778.80 |
kg/m3 |
293.15 |
Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
|
| ρl |
779.00 |
kg/m3 |
293.15 |
Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
|
| ρl |
778.70 |
kg/m3 |
293.15 |
Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
|
| ρl |
778.71 |
kg/m3 |
293.15 |
Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
|
| ρl |
778.41 |
kg/m3 |
293.15 |
Isothermal (vapour + liquid) equilibria for binary mixtures of diisopropyl ether with (methanol, or ethanol, or 1-butanol): Experimental data, correlations, and predictions
|
| ρl |
778.00 |
kg/m3 |
293.15 |
Volume expansion prediction of supercritical CO 2 + crude oil
|
| ρl |
778.51 |
kg/m3 |
293.15 |
Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
|
| ρl |
778.50 |
kg/m3 |
293.15 |
Partial molar volume of paracetamol in water, 0.1 M HCl and 0.154 M NaCl at T = (298.15, 303.15, 308.15 and 310.65) K and at 101.325 kPa
|
| ρl |
773.88 |
kg/m3 |
298.10 |
Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
|
| ρl |
774.00 |
kg/m3 |
298.15 |
Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K
|
| ρl |
773.81 |
kg/m3 |
298.15 |
Volumetric investigation of the ternary system ethanol + dimethylformamide + cyclohexane at 298.15 K
|
| ρl |
773.86 |
kg/m3 |
298.15 |
Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
|
| ρl |
773.92 |
kg/m3 |
298.15 |
Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
|
| ρl |
773.87 |
kg/m3 |
298.15 |
Thermodynamic properties of solvation of aromatic compounds in cyclohexane, heptane, benzene, 1,4-dioxane, and chloroform at 298.15 K
|
| ρl |
773.84 |
kg/m3 |
298.15 |
Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
|
| ρl |
776.11 |
kg/m3 |
298.15 |
Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
|
| ρl |
774.02 |
kg/m3 |
298.15 |
Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
|
| ρl |
774.00 |
kg/m3 |
298.15 |
Liquid-Liquid Equilibrium for 2,2,2-Trifluoroethanol + Ethanol + Cyclohexane from (288.15 to 308.15) K
|
| ρl |
773.88 |
kg/m3 |
298.15 |
Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
|
| ρl |
773.94 |
kg/m3 |
298.15 |
Excess molar volumes and excess isentropic compressibilities of binary and ternary mixtures of o-chlorotoluene with cyclic ether and amides or cyclohexane at different temperatures
|
| ρl |
773.94 |
kg/m3 |
298.15 |
Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
|
| ρl |
773.82 |
kg/m3 |
298.15 |
Solvation of N-methyl-2-pyrrolidone and N,N-dimethylpropanamide in cyclohexane, heptane, n-alkan-1-ols(C1-C4) and water at 298.15K
|
| ρl |
773.50 |
kg/m3 |
298.15 |
Measurements and modeling of LLE and HE for (methanol + 2,4,4-trimethyl-1-pentene), and LLE for (water + methanol + 2,4,4-trimethyl-1-pentene)
|
| ρl |
773.87 |
kg/m3 |
298.15 |
Volumetric, acoustic, and refractometric properties of (thiophene + hexane/cyclohexane) solutions in the presence of some imidazolium based ionic liquids at T = 298.15 K
|
| ρl |
774.00 |
kg/m3 |
298.15 |
Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)
|
| ρl |
773.86 |
kg/m3 |
298.15 |
Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
|
| ρl |
773.90 |
kg/m3 |
298.15 |
Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
|
| ρl |
773.88 |
kg/m3 |
298.15 |
(Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
|
| ρl |
773.96 |
kg/m3 |
298.15 |
Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
|
| ρl |
773.80 |
kg/m3 |
298.15 |
Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
|
| ρl |
773.94 |
kg/m3 |
298.15 |
Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
|
| ρl |
773.86 |
kg/m3 |
298.15 |
Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
|
| ρl |
773.93 |
kg/m3 |
298.15 |
Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
|
| ρl |
773.65 |
kg/m3 |
298.15 |
Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
|
| ρl |
773.70 |
kg/m3 |
298.15 |
Fluid Phase Topology of Benzene + Cyclohexane + 1-Propanol at 101.3 kPa
|
| ρl |
774.00 |
kg/m3 |
298.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
773.98 |
kg/m3 |
298.15 |
Vapor-Liquid Equilibria and Excess Enthalpies for Binary Systems of Dimethoxymethane with Hydrocarbons
|
| ρl |
773.92 |
kg/m3 |
298.15 |
Excess Enthalpies of the Ternary Mixtures: Tetrahydrofuran + (Hexane or Cyclohexane) + Decane at 298.15K
|
| ρl |
773.90 |
kg/m3 |
298.15 |
Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
|
| ρl |
773.80 |
kg/m3 |
298.15 |
Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
|
| ρl |
775.00 |
kg/m3 |
298.15 |
Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
|
| ρl |
773.78 |
kg/m3 |
298.15 |
Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
|
| ρl |
773.89 |
kg/m3 |
298.15 |
Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
|
| ρl |
773.90 |
kg/m3 |
298.15 |
Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
|
| ρl |
779.00 |
kg/m3 |
298.15 |
Liquid Liquid Equilibrium data for the ternary systems of Water, Isopropyl alcohol, and selected entrainers
|
| ρl |
773.85 |
kg/m3 |
298.20 |
Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
|
| ρl |
769.13 |
kg/m3 |
303.00 |
Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
|
| ρl |
768.80 |
kg/m3 |
303.15 |
Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
|
| ρl |
769.00 |
kg/m3 |
303.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
769.12 |
kg/m3 |
303.15 |
Volumetric and transport properties of ternary mixtures containing 1-propanol + ethyl ethanoate + cyclohexane or benzene at 303.15 K: Experimental data, correlation and prediction by ERAS model
|
| ρl |
768.90 |
kg/m3 |
303.15 |
Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
|
| ρl |
769.12 |
kg/m3 |
303.15 |
Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
|
| ρl |
769.10 |
kg/m3 |
303.15 |
Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
|
| ρl |
769.11 |
kg/m3 |
303.15 |
Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
|
| ρl |
769.30 |
kg/m3 |
303.15 |
Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
|
| ρl |
769.21 |
kg/m3 |
303.15 |
Excess molar volumes and excess isentropic compressibilities of binary and ternary mixtures of o-chlorotoluene with cyclic ether and amides or cyclohexane at different temperatures
|
| ρl |
769.30 |
kg/m3 |
303.15 |
Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
|
| ρl |
769.12 |
kg/m3 |
303.15 |
Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
|
| ρl |
769.00 |
kg/m3 |
303.15 |
Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
|
| ρl |
763.70 |
kg/m3 |
305.90 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
765.00 |
kg/m3 |
308.15 |
Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
|
| ρl |
764.50 |
kg/m3 |
308.15 |
Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
|
| ρl |
764.00 |
kg/m3 |
308.15 |
Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
|
| ρl |
764.35 |
kg/m3 |
308.15 |
Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
|
| ρl |
764.36 |
kg/m3 |
308.15 |
Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
|
| ρl |
764.45 |
kg/m3 |
308.15 |
Excess molar volumes and excess isentropic compressibilities of binary and ternary mixtures of o-chlorotoluene with cyclic ether and amides or cyclohexane at different temperatures
|
| ρl |
764.38 |
kg/m3 |
308.15 |
Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
|
| ρl |
764.30 |
kg/m3 |
308.15 |
Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
|
| ρl |
759.60 |
kg/m3 |
313.00 |
Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
|
| ρl |
759.52 |
kg/m3 |
313.15 |
Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
|
| ρl |
760.00 |
kg/m3 |
313.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
760.00 |
kg/m3 |
313.15 |
Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
|
| ρl |
759.41 |
kg/m3 |
313.15 |
Thermodynamic properties of cyclohexane methanol liquid mixture from shear viscosity measurements
|
| ρl |
759.80 |
kg/m3 |
313.15 |
Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
|
| ρl |
759.70 |
kg/m3 |
313.15 |
Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
|
| ρl |
759.20 |
kg/m3 |
313.15 |
Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
|
| ρl |
759.56 |
kg/m3 |
313.15 |
Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
|
| ρl |
759.30 |
kg/m3 |
313.15 |
Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
|
| ρl |
759.00 |
kg/m3 |
313.15 |
Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
|
| ρl |
759.57 |
kg/m3 |
313.15 |
Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
|
| ρl |
754.40 |
kg/m3 |
318.15 |
Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
|
| ρl |
754.74 |
kg/m3 |
318.15 |
Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
|
| ρl |
754.60 |
kg/m3 |
318.15 |
Thermodynamic properties of cyclohexane methanol liquid mixture from shear viscosity measurements
|
| ρl |
749.94 |
kg/m3 |
323.00 |
Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
|
| ρl |
751.00 |
kg/m3 |
323.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
748.70 |
kg/m3 |
323.15 |
Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
|
| ρl |
749.88 |
kg/m3 |
323.15 |
Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
|
| ρl |
749.50 |
kg/m3 |
323.15 |
Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
|
| ρl |
749.76 |
kg/m3 |
323.15 |
Thermodynamic properties of cyclohexane methanol liquid mixture from shear viscosity measurements
|
| ρl |
752.10 |
kg/m3 |
324.90 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
741.00 |
kg/m3 |
333.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
731.00 |
kg/m3 |
343.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
731.80 |
kg/m3 |
351.00 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
704.30 |
kg/m3 |
375.00 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
686.70 |
kg/m3 |
394.80 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
666.50 |
kg/m3 |
416.60 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
646.20 |
kg/m3 |
431.90 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
620.20 |
kg/m3 |
452.40 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
595.50 |
kg/m3 |
475.10 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
573.50 |
kg/m3 |
488.40 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
546.30 |
kg/m3 |
504.40 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
527.50 |
kg/m3 |
513.90 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
510.30 |
kg/m3 |
522.60 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
487.00 |
kg/m3 |
531.90 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
454.50 |
kg/m3 |
543.00 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
426.20 |
kg/m3 |
553.20 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
365.60 |
kg/m3 |
561.70 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
259.50 |
kg/m3 |
572.10 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
187.00 |
kg/m3 |
584.20 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
167.00 |
kg/m3 |
592.50 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
149.30 |
kg/m3 |
603.60 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
133.00 |
kg/m3 |
618.80 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
118.30 |
kg/m3 |
635.00 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
109.80 |
kg/m3 |
654.20 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
96.50 |
kg/m3 |
672.30 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
92.00 |
kg/m3 |
687.50 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| ρl |
89.90 |
kg/m3 |
698.50 |
Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
|
| D*i |
[0.00; 0.00] |
m2/s |
[308.16; 328.15] |
|
|
|
| D*i |
0.00 |
m2/s |
308.16 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
308.17 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
318.22 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
318.25 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
328.13 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
328.15 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| ΔfusS |
[9.57; 36.20] |
J/mol×K |
[186.10; 279.80] |
|
| ΔfusS |
36.20 |
J/mol×K |
186.10 |
NIST
|
| ΔfusS |
9.57 |
J/mol×K |
279.80 |
NIST
|
| csound,fluid |
[1133.70; 1327.80] |
m/s |
[283.15; 323.15] |
|
|
|
| csound,fluid |
1327.80 |
m/s |
283.15 |
Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
|
| csound,fluid |
1278.60 |
m/s |
293.15 |
Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
|
| csound,fluid |
1279.00 |
m/s |
293.15 |
Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
|
| csound,fluid |
1278.55 |
m/s |
293.15 |
Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
|
| csound,fluid |
1254.40 |
m/s |
298.15 |
Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
|
| csound,fluid |
1254.00 |
m/s |
298.15 |
Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
|
| csound,fluid |
1255.00 |
m/s |
298.15 |
Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 K
|
| csound,fluid |
1253.86 |
m/s |
298.15 |
Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
|
| csound,fluid |
1253.90 |
m/s |
298.15 |
Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
|
| csound,fluid |
1229.34 |
m/s |
303.15 |
Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
|
| csound,fluid |
1229.30 |
m/s |
303.15 |
Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
|
| csound,fluid |
1212.00 |
m/s |
308.15 |
Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 K
|
| csound,fluid |
1205.05 |
m/s |
308.15 |
Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
|
| csound,fluid |
1205.10 |
m/s |
308.15 |
Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
|
| csound,fluid |
1212.00 |
m/s |
308.15 |
Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
|
| csound,fluid |
1181.03 |
m/s |
313.15 |
Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
|
| csound,fluid |
1181.00 |
m/s |
313.15 |
Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
|
| csound,fluid |
1181.10 |
m/s |
313.15 |
Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
|
| csound,fluid |
1157.29 |
m/s |
318.15 |
Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
|
| csound,fluid |
1157.30 |
m/s |
318.15 |
Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
|
| csound,fluid |
1133.73 |
m/s |
323.15 |
Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
|
| csound,fluid |
1133.70 |
m/s |
323.15 |
Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
|
| γ |
[0.02; 0.03] |
N/m |
[279.33; 337.93] |
|
|
|
| γ |
0.03 |
N/m |
279.33 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
282.82 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
283.15 |
Thermophysical study of 1,4-dioxane with cycloalkane mixtures
|
| γ |
0.03 |
N/m |
287.81 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
288.15 |
Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
|
| γ |
0.03 |
N/m |
293.15 |
Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
|
| γ |
0.03 |
N/m |
293.15 |
Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
|
| γ |
0.03 |
N/m |
293.20 |
KDB
|
| γ |
0.02 |
N/m |
297.82 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.02 |
N/m |
298.15 |
Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
|
| γ |
0.02 |
N/m |
298.15 |
Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
|
| γ |
0.02 |
N/m |
298.15 |
Thermophysical study of 1,4-dioxane with cycloalkane mixtures
|
| γ |
0.02 |
N/m |
298.15 |
Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
|
| γ |
0.02 |
N/m |
303.15 |
Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
|
| γ |
0.02 |
N/m |
303.15 |
Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
|
| γ |
0.02 |
N/m |
307.86 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.02 |
N/m |
308.15 |
Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
|
| γ |
0.02 |
N/m |
308.15 |
Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
|
| γ |
0.02 |
N/m |
308.15 |
Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
|
| γ |
0.02 |
N/m |
313.15 |
Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
|
| γ |
0.02 |
N/m |
313.15 |
Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
|
| γ |
0.02 |
N/m |
313.15 |
Thermophysical study of 1,4-dioxane with cycloalkane mixtures
|
| γ |
0.02 |
N/m |
317.86 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.02 |
N/m |
318.15 |
Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
|
| γ |
0.02 |
N/m |
318.15 |
Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
|
| γ |
0.02 |
N/m |
318.15 |
Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
|
| γ |
0.02 |
N/m |
323.15 |
Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
|
| γ |
0.02 |
N/m |
323.15 |
Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
|
| γ |
0.02 |
N/m |
327.88 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.02 |
N/m |
328.15 |
Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
|
| γ |
0.02 |
N/m |
337.93 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| ΔvapS |
111.80 |
J/mol×K |
298.15 |
NIST
|
| λ |
[0.11; 0.12] |
W/m×K |
[280.83; 318.95] |
|
|
|
| λ |
0.12 |
W/m×K |
280.83 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.12 |
W/m×K |
281.00 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.12 |
W/m×K |
281.15 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.12 |
W/m×K |
295.53 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.12 |
W/m×K |
295.70 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.12 |
W/m×K |
295.83 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.12 |
W/m×K |
300.84 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.12 |
W/m×K |
301.00 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.12 |
W/m×K |
301.14 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.11 |
W/m×K |
318.66 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.11 |
W/m×K |
318.82 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
| λ |
0.11 |
W/m×K |
318.95 |
Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
|
