| Property |
Value |
Unit |
Temperature (K) |
Source |
| Cp,gas |
[130.08; 171.46] |
J/mol×K |
[371.20; 500.20] |
|
|
|
| Cp,gas |
130.08 ± 0.26 |
J/mol×K |
371.20 |
NIST
|
| Cp,gas |
140.20 |
J/mol×K |
390.00 |
NIST
|
| Cp,gas |
137.20 ± 1.30 |
J/mol×K |
393.00 |
NIST
|
| Cp,gas |
138.87 ± 0.27 |
J/mol×K |
396.20 |
NIST
|
| Cp,gas |
146.40 |
J/mol×K |
410.00 |
NIST
|
| Cp,gas |
149.16 ± 0.30 |
J/mol×K |
427.20 |
NIST
|
| Cp,gas |
149.40 ± 1.70 |
J/mol×K |
428.00 |
NIST
|
| Cp,gas |
160.33 ± 0.32 |
J/mol×K |
462.20 |
NIST
|
| Cp,gas |
159.00 ± 1.70 |
J/mol×K |
463.00 |
NIST
|
| Cp,gas |
171.46 ± 0.34 |
J/mol×K |
500.20 |
NIST
|
| Cp,liquid |
[138.39; 175.10] |
J/mol×K |
[228.15; 353.20] |
|
|
|
| Cp,liquid |
139.13 |
J/mol×K |
228.15 |
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
|
| Cp,liquid |
138.39 |
J/mol×K |
228.15 |
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
|
| Cp,liquid |
140.97 |
J/mol×K |
238.15 |
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
|
| Cp,liquid |
140.79 |
J/mol×K |
238.15 |
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
|
| Cp,liquid |
157.65 |
J/mol×K |
303.15 |
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
|
| Cp,liquid |
159.03 |
J/mol×K |
303.15 |
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
|
| Cp,liquid |
159.10 |
J/mol×K |
303.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
160.40 |
J/mol×K |
308.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
161.98 |
J/mol×K |
313.15 |
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
|
| Cp,liquid |
162.35 |
J/mol×K |
313.15 |
Isobaric Heat Capacity Measurements of Liquid Methane, Ethane, and Propane by Differential Scanning Calorimetry at High Pressures and Low Temperatures
|
| Cp,liquid |
161.60 |
J/mol×K |
313.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
163.00 |
J/mol×K |
318.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
164.10 |
J/mol×K |
323.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
165.50 |
J/mol×K |
328.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
167.00 |
J/mol×K |
333.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
168.60 |
J/mol×K |
338.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
170.40 |
J/mol×K |
343.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
172.80 |
J/mol×K |
348.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| Cp,liquid |
175.10 |
J/mol×K |
353.20 |
Heat capacities of aqueous binary and ternary mixtures (with piperazine) of N-(2-aminoethyl)-piperazine and N,N,N'-trimethylethylenediamine at temperatures (303.2-353.2) K
|
| η |
[0.0002860; 0.0006657] |
Pa×s |
[283.15; 363.15] |
|
|
|
| η |
0.0006657 |
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 |
0.0006300 |
Pa×s |
288.15 |
Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
|
| η |
0.0005880 |
Pa×s |
293.15 |
Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
|
| η |
0.0005958 |
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 |
0.0005531 |
Pa×s |
298.15 |
Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
|
| η |
0.0005635 |
Pa×s |
298.15 |
Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
|
| η |
0.0005560 |
Pa×s |
298.15 |
Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
|
| η |
0.0005530 |
Pa×s |
298.15 |
Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
|
| η |
0.0005540 |
Pa×s |
298.15 |
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
|
| η |
0.0005580 |
Pa×s |
298.15 |
Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
|
| η |
0.0005635 |
Pa×s |
298.15 |
Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
|
| η |
0.0005540 |
Pa×s |
298.15 |
Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
|
| η |
0.0005530 |
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 |
0.0005500 |
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 |
0.0005635 |
Pa×s |
298.15 |
Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
|
| η |
0.0005230 |
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 |
0.0005260 |
Pa×s |
303.15 |
Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
|
| η |
0.0005344 |
Pa×s |
303.15 |
Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
|
| η |
0.0005220 |
Pa×s |
303.15 |
Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
|
| η |
0.0005250 |
Pa×s |
303.15 |
Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
|
| η |
0.0005344 |
Pa×s |
303.15 |
Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
|
| η |
0.0005230 |
Pa×s |
303.15 |
Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
|
| η |
0.0005253 |
Pa×s |
303.15 |
Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
|
| η |
0.0005250 |
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 |
0.0005368 |
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 |
0.0005251 |
Pa×s |
303.15 |
Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
|
| η |
0.0005250 |
Pa×s |
303.15 |
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
|
| η |
0.0005344 |
Pa×s |
303.15 |
Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
|
| η |
0.0005020 |
Pa×s |
308.15 |
Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
|
| η |
0.0004980 |
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 |
0.0004933 |
Pa×s |
308.15 |
Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
|
| η |
0.0005091 |
Pa×s |
308.15 |
Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
|
| η |
0.0005091 |
Pa×s |
308.15 |
Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
|
| η |
0.0004960 |
Pa×s |
308.15 |
Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
|
| η |
0.0004940 |
Pa×s |
308.15 |
Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
|
| η |
0.0005091 |
Pa×s |
308.15 |
Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
|
| η |
0.0004990 |
Pa×s |
308.15 |
Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
|
| η |
0.0004710 |
Pa×s |
313.15 |
Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
|
| η |
0.0004700 |
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 |
0.0004755 |
Pa×s |
313.15 |
Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
|
| η |
0.0004710 |
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 |
0.0004700 |
Pa×s |
313.15 |
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
|
| η |
0.0004676 |
Pa×s |
313.15 |
Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
|
| η |
0.0004859 |
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 |
0.0004670 |
Pa×s |
313.15 |
Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
|
| η |
0.0004717 |
Pa×s |
313.15 |
Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
|
| η |
0.0004700 |
Pa×s |
313.15 |
Density and Viscosity Studies of Binary Mixtures of N,N-Dimethylformamide with Toluene and Methyl Benzoate at (298.15, 303.15, 308.15, and 313.15) K
|
| η |
0.0004491 |
Pa×s |
318.15 |
Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
|
| η |
0.0004379 |
Pa×s |
318.15 |
Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
|
| η |
0.0004460 |
Pa×s |
318.15 |
Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
|
| η |
0.0004230 |
Pa×s |
323.15 |
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
|
| η |
0.0004229 |
Pa×s |
323.15 |
Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
|
| η |
0.0004220 |
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 |
0.0004408 |
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 |
0.0004210 |
Pa×s |
323.15 |
Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
|
| η |
0.0004230 |
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 |
0.0004244 |
Pa×s |
323.15 |
Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
|
| η |
0.0004082 |
Pa×s |
328.15 |
Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
|
| η |
0.0003835 |
Pa×s |
333.15 |
Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
|
| η |
0.0003850 |
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
|
| η |
0.0003850 |
Pa×s |
333.15 |
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
|
| η |
0.0003810 |
Pa×s |
333.15 |
Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
|
| η |
0.0003500 |
Pa×s |
343.15 |
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
|
| η |
0.0003500 |
Pa×s |
343.15 |
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 |
0.0003490 |
Pa×s |
343.15 |
Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
|
| η |
0.0003100 |
Pa×s |
353.15 |
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
|
| η |
0.0003230 |
Pa×s |
353.15 |
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 |
0.0003210 |
Pa×s |
353.15 |
Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
|
| η |
0.0002860 |
Pa×s |
363.15 |
Densities and Viscosities of Diethyl Carbonate + Toluene, + Methanol, and + 2-Propanol from (293.15 to 363.15) K
|
| ΔfusH |
[6.55; 6.64] |
kJ/mol |
[177.95; 178.15] |
|
|
|
| ΔfusH |
6.62 |
kJ/mol |
177.95 |
NIST
|
| ΔfusH |
6.55 |
kJ/mol |
178.00 |
NIST
|
| ΔfusH |
6.61 |
kJ/mol |
178.00 |
NIST
|
| ΔfusH |
6.62 |
kJ/mol |
178.00 |
NIST
|
| ΔfusH |
6.64 |
kJ/mol |
178.15 |
NIST
|
| ΔvapH |
[24.00; 40.60] |
kJ/mol |
[244.50; 561.00] |
|
|
|
| ΔvapH |
40.60 |
kJ/mol |
244.50 |
NIST
|
| ΔvapH |
37.80 |
kJ/mol |
251.50 |
NIST
|
| ΔvapH |
38.90 |
kJ/mol |
284.00 |
NIST
|
| ΔvapH |
38.02 |
kJ/mol |
298.00 |
Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
|
| ΔvapH |
38.80 |
kJ/mol |
298.00 |
NIST
|
| ΔvapH |
36.90 |
kJ/mol |
318.00 |
NIST
|
| ΔvapH |
37.30 |
kJ/mol |
323.00 |
NIST
|
| ΔvapH |
37.80 |
kJ/mol |
324.00 |
NIST
|
| ΔvapH |
35.40 |
kJ/mol |
333.00 |
NIST
|
| ΔvapH |
35.65 |
kJ/mol |
341.27 |
NIST
|
| ΔvapH |
37.00 |
kJ/mol |
346.00 |
NIST
|
| ΔvapH |
37.00 |
kJ/mol |
347.00 |
NIST
|
| ΔvapH |
35.40 |
kJ/mol |
363.00 |
NIST
|
| ΔvapH |
33.40 |
kJ/mol |
373.00 |
NIST
|
| ΔvapH |
33.50 ± 0.10 |
kJ/mol |
380.00 |
NIST
|
| ΔvapH |
33.18 |
kJ/mol |
383.70 |
KDB
|
| ΔvapH |
33.18 |
kJ/mol |
383.80 |
NIST
|
| ΔvapH |
32.10 ± 0.10 |
kJ/mol |
403.00 |
NIST
|
| ΔvapH |
31.40 |
kJ/mol |
413.00 |
NIST
|
| ΔvapH |
35.70 |
kJ/mol |
413.50 |
NIST
|
| ΔvapH |
34.40 |
kJ/mol |
414.00 |
NIST
|
| ΔvapH |
29.40 ± 0.10 |
kJ/mol |
441.00 |
NIST
|
| ΔvapH |
28.40 |
kJ/mol |
453.00 |
NIST
|
| ΔvapH |
27.10 ± 0.10 |
kJ/mol |
470.00 |
NIST
|
| ΔvapH |
33.20 |
kJ/mol |
485.50 |
NIST
|
| ΔvapH |
24.00 |
kJ/mol |
493.00 |
NIST
|
| ΔvapH |
24.00 ± 0.10 |
kJ/mol |
505.00 |
NIST
|
| ΔvapH |
33.30 |
kJ/mol |
561.00 |
NIST
|
| Pvap |
[0.24; 3280.00] |
kPa |
[253.83; 573.20] |
|
|
|
| Pvap |
0.24 |
kPa |
253.83 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
0.47 |
kPa |
263.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
0.48 |
kPa |
263.64 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
0.48 |
kPa |
263.64 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
0.43 |
kPa |
263.75 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
0.91 |
kPa |
273.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
0.91 |
kPa |
273.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
0.93 |
kPa |
273.47 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
0.93 |
kPa |
273.47 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
0.84 |
kPa |
273.47 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
1.26 |
kPa |
278.70 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
1.67 |
kPa |
283.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
1.67 |
kPa |
283.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
1.68 |
kPa |
283.32 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
1.68 |
kPa |
283.32 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
1.57 |
kPa |
283.35 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
1.70 |
kPa |
283.60 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
2.42 |
kPa |
288.15 |
Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
|
| Pvap |
2.35 |
kPa |
288.15 |
Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
|
| Pvap |
2.26 |
kPa |
288.50 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
2.91 |
kPa |
293.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
3.18 |
kPa |
293.15 |
Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
|
| Pvap |
3.05 |
kPa |
293.15 |
Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
|
| Pvap |
2.91 |
kPa |
293.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
2.93 |
kPa |
293.24 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
2.93 |
kPa |
293.24 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
2.93 |
kPa |
293.26 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
2.82 |
kPa |
293.29 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
2.97 |
kPa |
293.40 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
3.78 |
kPa |
298.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
3.80 |
kPa |
298.15 |
(Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
|
| Pvap |
3.84 |
kPa |
298.15 |
Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
|
| Pvap |
3.80 |
kPa |
298.25 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
3.80 |
kPa |
298.25 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
3.89 |
kPa |
298.30 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
4.47 |
kPa |
300.89 |
Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
|
| Pvap |
4.87 |
kPa |
303.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
4.73 |
kPa |
303.15 |
Experimental Measurement and Modeling of Phase Diagrams of Binary Systems Encountered in the Gasoline Desulfurization Process Using Ionic Liquids
|
| Pvap |
4.90 |
kPa |
303.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
4.87 |
kPa |
303.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
4.87 |
kPa |
303.15 |
Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
|
| Pvap |
5.00 |
kPa |
303.20 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
4.90 |
kPa |
303.21 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
4.89 |
kPa |
303.23 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
4.90 |
kPa |
303.23 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
4.89 |
kPa |
303.23 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
4.79 |
kPa |
303.28 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
5.17 |
kPa |
305.64 |
Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
|
| Pvap |
5.23 |
kPa |
305.68 |
Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
|
| Pvap |
6.27 |
kPa |
308.10 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
6.32 |
kPa |
308.15 |
Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
|
| Pvap |
6.26 |
kPa |
308.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
7.99 |
kPa |
313.10 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
7.96 |
kPa |
313.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
7.88 |
kPa |
313.15 |
Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
|
| Pvap |
7.85 |
kPa |
313.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
7.85 |
kPa |
313.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
7.88 |
kPa |
313.15 |
Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
|
| Pvap |
7.88 |
kPa |
313.15 |
Isothermal vapor liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1- hexene + methylbenzene at 313.15 K
|
| Pvap |
7.89 |
kPa |
313.15 |
Phase equilibrium properties of the ternary mixture dibutyl ether + toluene + heptane at 313.15 K
|
| Pvap |
7.78 |
kPa |
313.15 |
Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
|
| Pvap |
7.87 |
kPa |
313.19 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
7.87 |
kPa |
313.19 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
8.10 |
kPa |
313.20 |
Isothermal vapor-liquid equilibrium of binary and ternary systems of anisole, hexane, and toluene and ternary system of methyl tert-butyl ether, hexane, and toluene
|
| Pvap |
7.87 |
kPa |
313.22 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
7.87 |
kPa |
313.22 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
7.79 |
kPa |
313.27 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
8.62 |
kPa |
315.15 |
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
|
| Pvap |
9.95 |
kPa |
318.00 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
9.89 |
kPa |
318.15 |
Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
|
| Pvap |
9.96 |
kPa |
318.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
10.77 |
kPa |
320.15 |
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
|
| Pvap |
12.26 |
kPa |
323.00 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
12.27 |
kPa |
323.15 |
Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
|
| Pvap |
12.31 |
kPa |
323.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
12.22 |
kPa |
323.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
12.23 |
kPa |
323.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
12.22 |
kPa |
323.15 |
Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
|
| Pvap |
12.29 |
kPa |
323.16 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
12.24 |
kPa |
323.22 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
12.25 |
kPa |
323.22 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
12.30 |
kPa |
323.25 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
13.40 |
kPa |
324.21 |
Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
|
| Pvap |
13.34 |
kPa |
325.15 |
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
|
| Pvap |
13.37 |
kPa |
325.16 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
14.53 |
kPa |
327.15 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
14.90 |
kPa |
327.60 |
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
|
| Pvap |
15.00 |
kPa |
327.90 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
14.96 |
kPa |
328.15 |
Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
|
| Pvap |
15.14 |
kPa |
328.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
15.77 |
kPa |
329.15 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
16.40 |
kPa |
330.15 |
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
|
| Pvap |
17.80 |
kPa |
332.15 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
18.26 |
kPa |
332.80 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
18.46 |
kPa |
333.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
18.56 |
kPa |
333.15 |
Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
|
| Pvap |
18.56 |
kPa |
333.15 |
An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
|
| Pvap |
18.45 |
kPa |
333.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
18.62 |
kPa |
333.15 |
Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
|
| Pvap |
18.86 |
kPa |
333.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
18.57 |
kPa |
333.20 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
18.57 |
kPa |
333.20 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
18.93 |
kPa |
333.22 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
19.35 |
kPa |
334.25 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
20.02 |
kPa |
335.15 |
Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
|
| Pvap |
20.00 |
kPa |
335.25 |
Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
|
| Pvap |
22.08 |
kPa |
337.65 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
22.04 |
kPa |
337.80 |
A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
|
| Pvap |
22.61 |
kPa |
338.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
23.83 |
kPa |
339.65 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
26.32 |
kPa |
342.30 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
26.47 |
kPa |
342.45 |
Vapor Pressure Measurements for Binary Mixtures Containing Ionic Liquid and Predictions by the Conductor-like Screening Model for Real Solvents
|
| Pvap |
26.66 |
kPa |
342.65 |
Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
|
| Pvap |
27.31 |
kPa |
343.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
27.10 |
kPa |
343.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
27.24 |
kPa |
343.15 |
An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
|
| Pvap |
27.12 |
kPa |
343.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
27.20 |
kPa |
343.16 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
27.20 |
kPa |
343.16 |
Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
|
| Pvap |
27.76 |
kPa |
343.18 |
Vapour liquid equilibria, enthalpy of mixing of binary mixtures containing diisopropylether DIPE and monoaromatic hydrocarbons Experimental results and modelling
|
| Pvap |
29.21 |
kPa |
345.25 |
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 |
32.72 |
kPa |
348.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
32.41 |
kPa |
348.15 |
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 |
37.22 |
kPa |
352.05 |
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 |
37.61 |
kPa |
352.25 |
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 |
38.84 |
kPa |
353.13 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
38.40 |
kPa |
353.15 |
Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
|
| Pvap |
38.87 |
kPa |
353.15 |
Isothermal vapour pressures and excess functions of 3,5- and 2,6-dimethylpyridine with toluene measurement and prediction
|
| Pvap |
38.84 |
kPa |
353.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
38.82 |
kPa |
353.15 |
An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
|
| Pvap |
38.92 |
kPa |
353.15 |
Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
|
| Pvap |
43.67 |
kPa |
356.65 |
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 |
45.96 |
kPa |
357.90 |
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 |
46.17 |
kPa |
358.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
49.60 |
kPa |
360.70 |
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
|
| Pvap |
51.35 |
kPa |
361.30 |
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 |
53.33 |
kPa |
362.63 |
Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
|
| Pvap |
53.30 |
kPa |
362.64 |
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 |
54.13 |
kPa |
363.08 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
54.49 |
kPa |
363.15 |
Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
|
| Pvap |
54.42 |
kPa |
363.15 |
Isothermal Vapor-Liquid Equilibria and Excess Enthalpy Data for the Binary System (Butyric Acid + Toluene)
|
| Pvap |
54.22 |
kPa |
363.15 |
An equipment for dynamic measurements of vapour liquid equilibria and results in binary systems containing cyclohexylamine
|
| Pvap |
55.59 |
kPa |
363.75 |
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 |
63.84 |
kPa |
368.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
63.48 |
kPa |
368.25 |
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 |
70.12 |
kPa |
371.40 |
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 |
79.99 |
kPa |
375.66 |
Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
|
| Pvap |
80.00 |
kPa |
375.66 |
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 |
79.30 |
kPa |
375.80 |
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
|
| Pvap |
82.48 |
kPa |
376.65 |
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 |
86.25 |
kPa |
378.15 |
Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
|
| Pvap |
95.30 |
kPa |
381.65 |
Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
|
| Pvap |
99.89 |
kPa |
383.25 |
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 |
101.30 |
kPa |
383.40 |
Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
|
| Pvap |
100.66 |
kPa |
383.50 |
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
|
| Pvap |
101.30 |
kPa |
383.55 |
Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
|
| Pvap |
101.30 |
kPa |
383.60 |
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 |
383.75 |
Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
|
| Pvap |
101.30 |
kPa |
383.76 |
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 |
383.77 |
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 |
101.30 |
kPa |
383.80 |
Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
|
| Pvap |
101.33 |
kPa |
383.81 |
Isobaric vapor-liquid equilibrium for binary system of cinnamaldehyde + benzaldehyde at 10, 20 and 30 kPa
|
| Pvap |
101.33 |
kPa |
383.82 |
Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
|
| Pvap |
102.00 |
kPa |
384.10 |
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 |
102.73 |
kPa |
384.30 |
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
|
| Pvap |
121.30 |
kPa |
390.25 |
Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
|
| Pvap |
121.30 |
kPa |
390.26 |
Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
|
| Pvap |
161.30 |
kPa |
400.75 |
Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
|
| Pvap |
201.30 |
kPa |
409.65 |
Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
|
| Pvap |
498.30 |
kPa |
451.00 |
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
|
| Pvap |
499.90 |
kPa |
451.50 |
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
|
| Pvap |
760.00 |
kPa |
473.30 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
760.00 |
kPa |
473.30 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
760.00 |
kPa |
473.30 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
1009.33 |
kPa |
490.40 |
Vapor pressure data of nicotine, anabasine and cotinine using differential scanning calorimetry
|
| Pvap |
1140.00 |
kPa |
498.30 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
1150.00 |
kPa |
498.30 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
1120.00 |
kPa |
498.30 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
1660.00 |
kPa |
523.40 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
1660.00 |
kPa |
523.40 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
1670.00 |
kPa |
523.40 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
2350.00 |
kPa |
548.30 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
2340.00 |
kPa |
548.40 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
2340.00 |
kPa |
548.40 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
3280.00 |
kPa |
573.20 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
3250.00 |
kPa |
573.20 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| Pvap |
3230.00 |
kPa |
573.20 |
A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
|
| n0 |
[1.48260; 1.50278] |
|
[283.15; 318.15] |
|
|
|
| n0 |
1.50278 |
|
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 |
1.49960 |
|
288.15 |
Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
|
| n0 |
1.49980 |
|
288.15 |
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.49980 |
|
288.15 |
Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.49600 |
|
293.00 |
Quaternary Liquid-Liquid Equilibrium of Water + Acetic Acid + Propionic Acid + Solvent (Amyl Alcohol, Cyclohexyl Acetate, or Toluene) Systems
|
| n0 |
1.49610 |
|
293.10 |
Vapor-Liquid Equilibria of Binary Systems Comprising 1-Chloro-2-ethylhexane and 2-Ethyl-1-hexanol
|
| n0 |
1.48730 |
|
293.10 |
Measurement and Correlation of Liquid-Liquid Equilibria of Methylcyclohexane + Toluene + N-Formylmorpholine at (293, 303, 313, and 323) K
|
| n0 |
1.48730 |
|
293.10 |
(Liquid + liquid) equilibria of three ternary systems: (heptane + benzene + N-formylmorpholine), (heptane + toluene + N-formylmorpholine), (heptane + xylene + N-formylmorpholine) from T = (298.15 to 353.15) K
|
| n0 |
1.49650 |
|
293.10 |
A study on densities and excess volumes in the (c-butyrolactone + aromatic hydrocarbon) system at various temperatures
|
| n0 |
1.49650 |
|
293.10 |
Densities and volumetric properties of N-methyl-2-pyrrolidone with aromatic hydrocarbon at different temperature
|
| n0 |
1.49700 |
|
293.15 |
Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.49700 |
|
293.15 |
Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
|
| n0 |
1.49650 |
|
293.15 |
A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
|
| n0 |
1.49670 |
|
293.15 |
Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
|
| n0 |
1.49670 |
|
293.15 |
Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
|
| n0 |
1.49670 |
|
293.15 |
Solubilities of Triphenylphosphine Oxide in Selected Solvents
|
| n0 |
1.49700 |
|
293.15 |
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.49687 |
|
293.15 |
Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
|
| n0 |
1.49600 |
|
293.15 |
Vapor liquid equilibria in ternary systems of associating components (water, aniline, cyclohexylamine) and hydrocarbons (octane or toluene)
|
| n0 |
1.49670 |
|
293.15 |
Solubilities of Phosphorus-Containing Compounds in Selected Solvents
|
| n0 |
1.49650 |
|
293.15 |
Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
|
| n0 |
1.49300 |
|
293.15 |
Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
|
| n0 |
1.49600 |
|
293.15 |
Ternary Liquid-Liquid(-Liquid) Equilibria of Aniline + Cyclohexylamine + Water, Aniline + Cyclohexylamine + Octane, Aniline + Water + Toluene, and Aniline + Water + Octane
|
| n0 |
1.49600 |
|
293.15 |
Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Water + Cyclohexylamine + Aromatic Hydrocarbon (Toluene or Propylbenzene) or Aliphatic Hydrocarbon (Heptane or Octane)
|
| n0 |
1.49690 |
|
293.15 |
Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
|
| n0 |
1.49620 |
|
293.15 |
Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
|
| n0 |
1.49650 |
|
293.15 |
Vapor-Liquid Equilibrium Measurements of MTBE and TAME with Toluene
|
| n0 |
1.49650 |
|
293.15 |
Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
|
| n0 |
1.49620 |
|
293.15 |
Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
|
| n0 |
1.49530 |
|
293.15 |
Isobaric (vapour + liquid) equilibria data for the binary systems {1,2-dichloroethane (1) + toluene (2)} and {1,2-dichloroethane (1) + acetic acid (2)} at atmospheric pressure
|
| n0 |
1.49670 |
|
293.20 |
Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
|
| n0 |
1.49393 |
|
298.10 |
Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
|
| n0 |
1.49410 |
|
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 |
1.49410 |
|
298.15 |
Excess molar volumes of (propiophenone + toluene) and estimated density of liquid propiophenone below its melting temperature
|
| n0 |
1.49399 |
|
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 |
1.49410 |
|
298.15 |
Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
|
| n0 |
1.49398 |
|
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 |
1.49399 |
|
298.15 |
Effect of the Chain Length on the Aromatic Ring in the Separation of Aromatic Compounds from Methylcyclohexane Using the Ionic Liquid 1-Ethyl-3-methylpyridinium Ethylsulfate
|
| n0 |
1.49393 |
|
298.15 |
Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
|
| n0 |
1.49393 |
|
298.15 |
Volumetric behavior of the ternary system (methyl tert-butyl ether + methylbenzene + butan-1-ol) and its binary sub-system (methyl tert-butyl ether + butan-1-ol) within the temperature range (298.15 to 328.15) K
|
| n0 |
1.49410 |
|
298.15 |
Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
|
| n0 |
1.49406 |
|
298.15 |
Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
|
| n0 |
1.49410 |
|
298.15 |
Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
|
| n0 |
1.49400 |
|
298.15 |
Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
|
| n0 |
1.49397 |
|
298.15 |
Isothermal vapor-liquid equilibrium at T = 333.15 K and excess volumes and molar refractivity deviation at T = 298.15 K for the ternary mixtures {di-methyl carbonate (DMC) + ethanol + benzene} and {DMC+ ethanol + toluene}
|
| n0 |
1.49410 |
|
298.15 |
Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
|
| n0 |
1.49410 |
|
298.15 |
Physical properties of (propyl propanoate + hexane + toluene) at 298.15 K
|
| n0 |
1.49397 |
|
298.15 |
Isothermal vapor liquid equilibrium at 333.15K and excess volumes and molar refractivity deviation at 298.15K for the ternary system di-butyl ether (1) + ethanol (2) + toluene (3) and its binary subsystems
|
| n0 |
1.49650 |
|
298.15 |
Densities and excess volumes of binary mixtures of N,N-dimethylformamide with aromatic hydrocarbon at different temperature
|
| n0 |
1.49419 |
|
298.15 |
Vapor-Liquid Equilibrium and Density of the Binary System 1-Phenylethylamine + Toluene
|
| n0 |
1.49390 |
|
298.15 |
Densities, speeds of sound, and refractive indices of the ternary mixtures (toluene + methyl acetate + butyl acetate) and (toluene + methyl acetate + methyl heptanoate) at 298.15 K
|
| n0 |
1.49399 |
|
298.15 |
Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
|
| n0 |
1.49399 |
|
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 |
1.49440 |
|
298.15 |
Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
|
| n0 |
1.49390 |
|
298.15 |
Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
|
| n0 |
1.49390 |
|
298.15 |
Vapor-Liquid Equilibrium for Binary System of Thiophene + n-Hexane at (338.15 and 323.15) K and Thiophene + 1-Hexene at (333.15 and 323.15) K
|
| n0 |
1.49390 |
|
298.15 |
Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
|
| n0 |
1.49420 |
|
298.15 |
Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
|
| n0 |
1.49390 |
|
298.15 |
Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Hexane at (338.15 and 323.15) K and Diethyl Sulfide + 1-Hexene at (333.15 and 323.15) K
|
| n0 |
1.49399 |
|
298.15 |
Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
|
| n0 |
1.49360 |
|
298.15 |
Experimental Isobaric Vapor-Liquid Equilibria of Binary Mixtures of 2,2,2-Trifluoroethanol with Benzene or Toluene
|
| n0 |
1.49399 |
|
298.15 |
Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
|
| n0 |
1.49400 |
|
298.15 |
Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
|
| n0 |
1.49413 |
|
298.15 |
KDB
|
| n0 |
1.49420 |
|
298.15 |
Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.49650 |
|
298.15 |
The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
|
| n0 |
1.49380 |
|
298.15 |
Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
|
| n0 |
1.49420 |
|
298.15 |
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.49310 |
|
298.15 |
Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
|
| n0 |
1.49390 |
|
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 |
1.49400 |
|
298.20 |
(Liquid + liquid) equilibria of aqueous solutions of butyric acid with n-heptane and toluene at T = (298.2, 308.2, and 318.2) K
|
| n0 |
1.49180 |
|
303.15 |
Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
|
| n0 |
1.49020 |
|
303.15 |
Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
|
| n0 |
1.49130 |
|
303.15 |
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.49124 |
|
303.15 |
Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
|
| n0 |
1.49140 |
|
303.15 |
Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
|
| n0 |
1.49130 |
|
303.15 |
Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.48850 |
|
308.15 |
Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
|
| n0 |
1.48840 |
|
308.15 |
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.48840 |
|
308.15 |
Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.48740 |
|
308.15 |
Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
|
| n0 |
1.48550 |
|
313.15 |
Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.48550 |
|
313.15 |
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.48260 |
|
318.15 |
Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
|
| n0 |
1.48260 |
|
318.15 |
Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
|
| ρl |
[781.97; 876.19] |
kg/m3 |
[283.15; 373.20] |
|
|
|
| ρl |
876.19 |
kg/m3 |
283.15 |
Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
|
| ρl |
871.44 |
kg/m3 |
288.15 |
Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
|
| ρl |
871.79 |
kg/m3 |
288.15 |
Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
|
| ρl |
871.00 |
kg/m3 |
288.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
871.50 |
kg/m3 |
288.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
871.92 |
kg/m3 |
288.20 |
The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
|
| ρl |
867.00 |
kg/m3 |
293.00 |
KDB
|
| ρl |
867.00 |
kg/m3 |
293.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
866.68 |
kg/m3 |
293.15 |
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
|
| ρl |
866.80 |
kg/m3 |
293.15 |
Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
|
| ρl |
866.70 |
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 |
866.84 |
kg/m3 |
293.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
|
| ρl |
866.70 |
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 |
866.82 |
kg/m3 |
293.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
|
| ρl |
867.08 |
kg/m3 |
293.15 |
Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
|
| ρl |
866.91 |
kg/m3 |
293.15 |
Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
|
| ρl |
866.82 |
kg/m3 |
293.15 |
Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
|
| ρl |
866.78 |
kg/m3 |
293.15 |
Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
|
| ρl |
866.98 |
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 |
866.84 |
kg/m3 |
293.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
866.92 |
kg/m3 |
293.15 |
Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
|
| ρl |
866.93 |
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 |
868.00 |
kg/m3 |
293.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
867.80 |
kg/m3 |
293.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
866.51 |
kg/m3 |
293.20 |
Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
|
| ρl |
867.61 |
kg/m3 |
293.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
866.81 |
kg/m3 |
293.20 |
Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure
|
| ρl |
867.30 |
kg/m3 |
293.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
864.69 |
kg/m3 |
295.20 |
Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
|
| ρl |
862.86 |
kg/m3 |
297.20 |
Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
|
| ρl |
857.61 |
kg/m3 |
298.00 |
Removal of aromatic hydrocarbons from hydrocarbon mixture using glycols at 303.15 K and 333.15 K and atmospheric pressure: Experimental and calculated data by NRTL and UNIQUAC models
|
| ρl |
866.90 |
kg/m3 |
298.15 |
Liquid-liquid equilibria for multicomponent mixtures of 2,2-dimethyl-1,3-dioxolane with n-heptane, toluene, ethanol and water
|
| ρl |
862.19 |
kg/m3 |
298.15 |
Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
|
| ρl |
862.21 |
kg/m3 |
298.15 |
Thermodynamic Properties of Ternary Liquid Mixtures of 2-Pyrrolidinone with Aromatic Hydrocarbons
|
| ρl |
862.11 |
kg/m3 |
298.15 |
Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K
|
| ρl |
862.21 |
kg/m3 |
298.15 |
Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
|
| ρl |
862.10 |
kg/m3 |
298.15 |
Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
|
| ρl |
862.21 |
kg/m3 |
298.15 |
Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
|
| ρl |
862.19 |
kg/m3 |
298.15 |
Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
|
| ρl |
862.36 |
kg/m3 |
298.15 |
Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
|
| ρl |
862.34 |
kg/m3 |
298.15 |
Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
|
| ρl |
857.58 |
kg/m3 |
298.15 |
Experimental and theoretical study of surface tension of binary mixtures of (n-alkyl acetates + heptane, benzene, and toluene)
|
| ρl |
863.67 |
kg/m3 |
298.15 |
Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
|
| ρl |
862.40 |
kg/m3 |
298.15 |
Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
|
| ρl |
861.81 |
kg/m3 |
298.15 |
Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
|
| ρl |
862.27 |
kg/m3 |
298.15 |
Mutual Solubility of Pyridinium-Based Tetrafluoroborates and Toluene
|
| ρl |
862.35 |
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 |
862.17 |
kg/m3 |
298.15 |
Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
|
| ρl |
862.17 |
kg/m3 |
298.15 |
Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
|
| ρl |
862.17 |
kg/m3 |
298.15 |
(Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
|
| ρl |
862.17 |
kg/m3 |
298.15 |
Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 K
|
| ρl |
862.23 |
kg/m3 |
298.15 |
Binary and Ternary Vapor-Liquid Equilibrium at 323.15 K and Excess Molar Volumes at 298.15 K for the Mixtures of Propyl Vinyl Ether + 1-Propanol + Toluene
|
| ρl |
862.23 |
kg/m3 |
298.15 |
Topological Investigations of Excess Molar Volumes and Excess Isentropic Compressibilities of Ternary Mixtures Containing Pyrrolidin-2-one at 308.15 K
|
| ρl |
862.23 |
kg/m3 |
298.15 |
Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
|
| ρl |
862.22 |
kg/m3 |
298.15 |
Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
|
| ρl |
862.23 |
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 |
862.20 |
kg/m3 |
298.15 |
Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
|
| ρl |
862.21 |
kg/m3 |
298.15 |
Conformational analysis of branched alkanes using limiting partial molar volumes
|
| ρl |
862.18 |
kg/m3 |
298.15 |
Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
|
| ρl |
862.18 |
kg/m3 |
298.15 |
Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
|
| ρl |
862.00 |
kg/m3 |
298.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
862.20 |
kg/m3 |
298.15 |
Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
|
| ρl |
862.18 |
kg/m3 |
298.15 |
Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
|
| ρl |
862.22 |
kg/m3 |
298.15 |
Excess Enthalpy and Excess Volume for Pyridine + Methyldiethanolamine and Pyridine + Ethanolamine Mixtures
|
| ρl |
866.90 |
kg/m3 |
298.15 |
Liquid-liquid equilibria for ternary mixtures of 2,2-dimethyl-1,3-dioxolane-4-methanol with n-heptane, toluene, ethanol and water
|
| ρl |
862.29 |
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 |
863.67 |
kg/m3 |
298.15 |
Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
|
| ρl |
862.18 |
kg/m3 |
298.15 |
Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
|
| ρl |
862.23 |
kg/m3 |
298.15 |
Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes at 298.15K for the ternary system di-isopropyl ether + n-propyl alcohol + toluene and its binary subsystems
|
| ρl |
862.18 |
kg/m3 |
298.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
862.00 |
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 |
864.99 |
kg/m3 |
298.15 |
Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
|
| ρl |
862.34 |
kg/m3 |
298.15 |
Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
|
| ρl |
862.23 |
kg/m3 |
298.15 |
Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) K
|
| ρl |
862.27 |
kg/m3 |
298.15 |
Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
|
| ρl |
862.00 |
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 |
862.10 |
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 |
862.18 |
kg/m3 |
298.15 |
Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
|
| ρl |
862.19 |
kg/m3 |
298.15 |
Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
|
| ρl |
861.74 |
kg/m3 |
298.15 |
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
|
| ρl |
862.35 |
kg/m3 |
298.15 |
Mutual Solubilities of Terpene in Methanol and Water and Their Multicomponent Liquid-Liquid Equilibria
|
| ρl |
862.27 |
kg/m3 |
298.15 |
Binary liquid liquid equilibrium in the systems containing monofunctional benzene derivates and 1,2-ethanediol
|
| ρl |
861.94 |
kg/m3 |
298.20 |
Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
|
| ρl |
862.49 |
kg/m3 |
298.20 |
The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
|
| ρl |
861.45 |
kg/m3 |
298.70 |
Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
|
| ρl |
857.64 |
kg/m3 |
303.15 |
Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
|
| ρl |
857.53 |
kg/m3 |
303.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
|
| ρl |
858.00 |
kg/m3 |
303.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
857.51 |
kg/m3 |
303.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
857.51 |
kg/m3 |
303.15 |
Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
|
| ρl |
857.47 |
kg/m3 |
303.15 |
Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
|
| ρl |
857.51 |
kg/m3 |
303.15 |
Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
|
| ρl |
857.50 |
kg/m3 |
303.15 |
Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
|
| ρl |
857.61 |
kg/m3 |
303.15 |
Measurement of phase equilibria data for the extraction of toluene from alkane using different solvents
|
| ρl |
857.50 |
kg/m3 |
303.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
|
| ρl |
857.39 |
kg/m3 |
303.15 |
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
|
| ρl |
857.50 |
kg/m3 |
303.15 |
Volumetric properties of binary liquid mixtures: Application of the Prigogine Flory Patterson theory to excess molar volumes of dichloromethane with benzene or toluene
|
| ρl |
857.58 |
kg/m3 |
303.15 |
Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
|
| ρl |
857.73 |
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 |
857.50 |
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 |
857.50 |
kg/m3 |
303.15 |
Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
|
| ρl |
856.12 |
kg/m3 |
303.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
855.94 |
kg/m3 |
303.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
855.63 |
kg/m3 |
303.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
851.69 |
kg/m3 |
308.15 |
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
|
| ρl |
852.82 |
kg/m3 |
308.15 |
Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
|
| ρl |
852.93 |
kg/m3 |
308.15 |
Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
|
| ρl |
852.80 |
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 |
852.83 |
kg/m3 |
308.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
852.79 |
kg/m3 |
308.15 |
Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
|
| ρl |
852.82 |
kg/m3 |
308.15 |
Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
|
| ρl |
848.15 |
kg/m3 |
313.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
848.11 |
kg/m3 |
313.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
|
| ρl |
848.80 |
kg/m3 |
313.15 |
Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
|
| ρl |
848.21 |
kg/m3 |
313.15 |
Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
|
| ρl |
848.00 |
kg/m3 |
313.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
848.14 |
kg/m3 |
313.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
|
| ρl |
848.00 |
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 |
848.11 |
kg/m3 |
313.15 |
Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
|
| ρl |
847.82 |
kg/m3 |
313.15 |
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
|
| ρl |
848.07 |
kg/m3 |
313.15 |
Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
|
| ρl |
848.20 |
kg/m3 |
313.15 |
Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
|
| ρl |
844.27 |
kg/m3 |
313.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
844.57 |
kg/m3 |
313.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
844.75 |
kg/m3 |
313.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
848.23 |
kg/m3 |
313.20 |
The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
|
| ρl |
843.44 |
kg/m3 |
318.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
842.88 |
kg/m3 |
318.15 |
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
|
| ρl |
843.49 |
kg/m3 |
318.15 |
Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
|
| ρl |
843.30 |
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 |
838.42 |
kg/m3 |
323.15 |
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
|
| ρl |
838.50 |
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 |
840.00 |
kg/m3 |
323.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
838.66 |
kg/m3 |
323.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
|
| ρl |
838.66 |
kg/m3 |
323.15 |
Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
|
| ρl |
838.90 |
kg/m3 |
323.15 |
Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
|
| ρl |
838.73 |
kg/m3 |
323.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
838.70 |
kg/m3 |
323.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
|
| ρl |
833.21 |
kg/m3 |
323.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
833.68 |
kg/m3 |
323.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
833.51 |
kg/m3 |
323.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
834.00 |
kg/m3 |
328.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
829.12 |
kg/m3 |
333.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
|
| ρl |
829.25 |
kg/m3 |
333.15 |
Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
|
| ρl |
829.13 |
kg/m3 |
333.15 |
Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
|
| ρl |
829.16 |
kg/m3 |
333.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
|
| ρl |
828.94 |
kg/m3 |
333.15 |
Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
|
| ρl |
829.60 |
kg/m3 |
333.15 |
Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
|
| ρl |
831.00 |
kg/m3 |
333.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
822.73 |
kg/m3 |
333.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
822.90 |
kg/m3 |
333.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
822.43 |
kg/m3 |
333.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
819.60 |
kg/m3 |
343.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
|
| ρl |
820.20 |
kg/m3 |
343.15 |
Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
|
| ρl |
819.51 |
kg/m3 |
343.15 |
Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
|
| ρl |
821.00 |
kg/m3 |
343.15 |
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
|
| ρl |
812.39 |
kg/m3 |
343.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
811.93 |
kg/m3 |
343.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
812.22 |
kg/m3 |
343.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
809.70 |
kg/m3 |
353.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
|
| ρl |
802.15 |
kg/m3 |
353.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
801.69 |
kg/m3 |
353.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
801.98 |
kg/m3 |
353.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
799.70 |
kg/m3 |
363.15 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
|
| ρl |
792.16 |
kg/m3 |
363.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
791.71 |
kg/m3 |
363.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
792.00 |
kg/m3 |
363.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
782.26 |
kg/m3 |
373.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
782.42 |
kg/m3 |
373.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| ρl |
781.97 |
kg/m3 |
373.20 |
Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
|
| D*i |
[0.00; 0.00] |
m2/s |
[239.09; 343.45] |
|
|
|
| D*i |
0.00 |
m2/s |
239.09 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
240.94 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
248.57 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
251.71 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
253.27 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
253.28 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
258.16 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
258.23 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
263.51 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
268.32 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
273.43 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
273.54 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
278.07 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
278.15 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
288.05 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
293.08 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
298.00 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
298.18 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
298.20 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
298.21 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
298.21 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
298.21 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
308.07 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
322.69 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
323.16 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
323.18 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
332.93 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
333.16 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| D*i |
0.00 |
m2/s |
343.45 |
Viscous Calibration Liquids for Self-diffusion Measurements
|
| ΔfusS |
[36.79; 37.25] |
J/mol×K |
[177.95; 178.15] |
|
| ΔfusS |
37.20 |
J/mol×K |
177.95 |
NIST
|
| ΔfusS |
36.79 |
J/mol×K |
178.00 |
NIST
|
| ΔfusS |
37.25 |
J/mol×K |
178.15 |
NIST
|
| csound,fluid |
[425.50; 1394.10] |
m/s |
[278.15; 523.15] |
|
|
|
| csound,fluid |
1394.10 |
m/s |
278.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1371.50 |
m/s |
283.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1347.50 |
m/s |
288.15 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1349.10 |
m/s |
288.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1347.50 |
m/s |
288.15 |
Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
|
| csound,fluid |
1336.32 |
m/s |
290.65 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1325.34 |
m/s |
293.15 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1326.90 |
m/s |
293.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1328.60 |
m/s |
293.15 |
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
|
| csound,fluid |
1314.33 |
m/s |
295.65 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1307.30 |
m/s |
298.15 |
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
|
| csound,fluid |
1303.00 |
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 |
1303.44 |
m/s |
298.15 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1305.10 |
m/s |
298.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1303.00 |
m/s |
298.15 |
Isentropic Compressibilities Changes of Mixing of Tetrahydropyran and Aromatic Hydrocarbons Ternary Mixtures at 308.15 K
|
| csound,fluid |
1304.00 |
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 |
1304.00 |
m/s |
298.15 |
Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
|
| csound,fluid |
1303.44 |
m/s |
298.15 |
Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
|
| csound,fluid |
1292.64 |
m/s |
300.65 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1283.60 |
m/s |
303.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1281.88 |
m/s |
303.15 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1285.50 |
m/s |
303.15 |
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
|
| csound,fluid |
1271.16 |
m/s |
305.65 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1262.00 |
m/s |
308.15 |
Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
|
| csound,fluid |
1262.20 |
m/s |
308.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1262.00 |
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 |
1262.00 |
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 |
1260.49 |
m/s |
308.15 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1264.20 |
m/s |
308.15 |
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
|
| csound,fluid |
1249.83 |
m/s |
310.65 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1240.90 |
m/s |
313.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1242.40 |
m/s |
313.15 |
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
|
| csound,fluid |
1239.22 |
m/s |
313.15 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1228.62 |
m/s |
315.65 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1220.70 |
m/s |
318.15 |
Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
|
| csound,fluid |
1219.90 |
m/s |
318.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1218.01 |
m/s |
318.15 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1207.31 |
m/s |
320.65 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1198.90 |
m/s |
323.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1196.60 |
m/s |
323.15 |
Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
|
| csound,fluid |
1200.80 |
m/s |
323.15 |
Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
|
| csound,fluid |
1196.60 |
m/s |
323.15 |
Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
|
| csound,fluid |
1200.80 |
m/s |
323.15 |
Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
|
| csound,fluid |
1178.20 |
m/s |
328.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1157.70 |
m/s |
333.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1137.20 |
m/s |
338.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1117.00 |
m/s |
343.15 |
Advanced calibration, adjustment, and operation of a density and sound speed analyzer
|
| csound,fluid |
1000.00 |
m/s |
373.15 |
Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
|
| csound,fluid |
806.00 |
m/s |
423.15 |
Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
|
| csound,fluid |
806.00 |
m/s |
423.15 |
Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
|
| csound,fluid |
616.20 |
m/s |
473.15 |
Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
|
| csound,fluid |
425.50 |
m/s |
523.15 |
Speed of sound measurement in ethyl tert-butyl ether and tert-amyl methyl ether by Brillouin light scattering
|
| csound,fluid |
425.50 |
m/s |
523.15 |
Measurement of the Speed of Sound in Hexane and Heptane at Temperatures from (303.15 to 536.15) K and Pressures from (1.0 to 8.5) MPa
|
| γ |
[0.02; 0.03] |
N/m |
[277.85; 368.14] |
|
|
|
| γ |
0.03 |
N/m |
277.85 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
278.15 |
Thermodynamic investigation of N,N-dimethylformamide/toluene binary mixtures in the temperature range from 278.15 to 293.15 K
|
| γ |
0.03 |
N/m |
283.15 |
Thermodynamic investigation of N,N-dimethylformamide/toluene binary mixtures in the temperature range from 278.15 to 293.15 K
|
| γ |
0.03 |
N/m |
287.81 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
288.15 |
Surface Tension of the Ternary System Water + Acetone + Toluene
|
| γ |
0.03 |
N/m |
293.00 |
Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Selected Ternary Mixtures of n-Butylcyclohexane + a Linear Alkane (n-Hexadcane or n-Dodecane) + an Aromatic Compound (Toluene, n-Butylbenzene, or n-Hexylbenzene)
|
| γ |
0.03 |
N/m |
293.15 |
Thermodynamic investigation of N,N-dimethylformamide/toluene binary mixtures in the temperature range from 278.15 to 293.15 K
|
| γ |
0.03 |
N/m |
293.20 |
KDB
|
| γ |
0.03 |
N/m |
297.82 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
298.15 |
Surface Tension of the Ternary System Water + Acetone + Toluene
|
| γ |
0.03 |
N/m |
302.83 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
303.16 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.03 |
N/m |
307.86 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
308.15 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.03 |
N/m |
308.15 |
Surface Tension of the Ternary System Water + Acetone + Toluene
|
| γ |
0.03 |
N/m |
312.87 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
313.15 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.03 |
N/m |
317.86 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.03 |
N/m |
318.13 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.03 |
N/m |
318.15 |
Surface Tension of the Ternary System Water + Acetone + Toluene
|
| γ |
0.02 |
N/m |
323.15 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
327.88 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.02 |
N/m |
328.15 |
Surface Tension of the Ternary System Water + Acetone + Toluene
|
| γ |
0.02 |
N/m |
328.16 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
333.14 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
337.88 |
Surface Tension of Pure Liquids and Binary Liquid Mixtures
|
| γ |
0.02 |
N/m |
338.16 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
343.16 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
348.16 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
353.15 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
358.15 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
363.16 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| γ |
0.02 |
N/m |
368.14 |
Surface tension of four oxygenated fuels: experiment and correlation
|
| λ |
[0.11; 0.15] |
W/m×K |
[234.60; 375.71] |
|
|
|
| λ |
0.15 |
W/m×K |
234.60 |
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
|
| λ |
0.14 |
W/m×K |
254.58 |
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
|
| λ |
0.14 |
W/m×K |
272.64 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.14 |
W/m×K |
273.17 |
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
|
| λ |
0.14 |
W/m×K |
273.45 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.14 |
W/m×K |
274.65 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.14 |
W/m×K |
275.40 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.14 |
W/m×K |
275.95 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.14 |
W/m×K |
276.19 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.14 |
W/m×K |
276.31 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
278.42 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.13 |
W/m×K |
281.25 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.13 |
W/m×K |
281.25 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.13 |
W/m×K |
287.33 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
288.72 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
289.65 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
293.23 |
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
|
| λ |
0.13 |
W/m×K |
294.45 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
294.69 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
295.01 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.13 |
W/m×K |
295.07 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.13 |
W/m×K |
295.08 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
295.47 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
295.79 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
297.45 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
298.60 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
300.43 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
302.05 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.13 |
W/m×K |
304.59 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.13 |
W/m×K |
307.66 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
308.62 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
310.22 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
314.68 |
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
|
| λ |
0.13 |
W/m×K |
314.69 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
314.74 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
315.55 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
315.85 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
316.70 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.13 |
W/m×K |
316.82 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.13 |
W/m×K |
317.94 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
318.80 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.12 |
W/m×K |
318.84 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.12 |
W/m×K |
319.32 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
319.96 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
321.21 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.12 |
W/m×K |
327.65 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
328.48 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.12 |
W/m×K |
329.50 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
329.65 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.12 |
W/m×K |
330.77 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
331.24 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.12 |
W/m×K |
333.34 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.12 |
W/m×K |
334.99 |
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
|
| λ |
0.12 |
W/m×K |
335.27 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.12 |
W/m×K |
337.36 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.12 |
W/m×K |
337.63 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.12 |
W/m×K |
338.23 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.12 |
W/m×K |
338.39 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
339.65 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.12 |
W/m×K |
339.77 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
339.85 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.12 |
W/m×K |
340.17 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.12 |
W/m×K |
340.62 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
341.16 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.12 |
W/m×K |
343.09 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.12 |
W/m×K |
346.01 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.12 |
W/m×K |
347.00 |
Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
|
| λ |
0.11 |
W/m×K |
350.87 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.12 |
W/m×K |
351.33 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.12 |
W/m×K |
351.55 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.12 |
W/m×K |
352.25 |
Thermal conductivity and thermal diffusivity of pyrrolidinium- based ionic liquids at atmospheric pressure
|
| λ |
0.11 |
W/m×K |
354.89 |
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
|
| λ |
0.11 |
W/m×K |
355.63 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.12 |
W/m×K |
355.71 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.11 |
W/m×K |
355.95 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.11 |
W/m×K |
357.02 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.11 |
W/m×K |
365.42 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.11 |
W/m×K |
370.29 |
Thermal conductivity of ethyl fluoride (HFC161)
|
| λ |
0.11 |
W/m×K |
373.92 |
Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
|
| λ |
0.11 |
W/m×K |
375.26 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.11 |
W/m×K |
375.26 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| λ |
0.11 |
W/m×K |
375.71 |
Thermal Conductivity of Liquid Dimethoxyethane from 243 to 353K at Pressures up to 30 MPa
|
| αdiff |
[4.66e-08; 8.63e-08] |
m2/s |
[302.90; 523.38] |
|
|
|
| αdiff |
8.63e-08 |
m2/s |
302.90 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
8.33e-08 |
m2/s |
312.45 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
8.03e-08 |
m2/s |
323.07 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
7.77e-08 |
m2/s |
333.27 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
7.52e-08 |
m2/s |
343.52 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
7.30e-08 |
m2/s |
353.73 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
7.09e-08 |
m2/s |
363.73 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
6.90e-08 |
m2/s |
373.04 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
6.71e-08 |
m2/s |
382.94 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
6.52e-08 |
m2/s |
392.88 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
6.33e-08 |
m2/s |
402.93 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
6.15e-08 |
m2/s |
413.06 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
5.98e-08 |
m2/s |
422.73 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
5.81e-08 |
m2/s |
432.67 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
5.64e-08 |
m2/s |
442.68 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
5.48e-08 |
m2/s |
452.96 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
5.33e-08 |
m2/s |
462.99 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
5.19e-08 |
m2/s |
473.20 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
5.06e-08 |
m2/s |
482.98 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
4.94e-08 |
m2/s |
493.05 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
4.84e-08 |
m2/s |
503.17 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
4.74e-08 |
m2/s |
513.41 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
| αdiff |
4.66e-08 |
m2/s |
523.38 |
Thermal Diffusivity of 2-Ethoxy-2-methylpropane (ETBE) and 2-Methoxy-2-methylbutane (TAME) at Temperatures from (293 to 523) K and Pressure up to 10 MPa
|
