- InChI
- InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
- InChI Key
- WYURNTSHIVDZCO-UHFFFAOYSA-N
- Formula
- C4H8O
- SMILES
- C1CCOC1
- Molecular Weight1
- 72.11
- CAS
- 109-99-9
- Other Names
-
- 1,4-epoxybutane
- Butane «alpha»,«delta»-oxide
- Butane, 1,4-epoxy-
- Cyclotetramethylene oxide
- Diethylene oxide
- Dynasolve 150
- Furan, tetrahydro-
- Furanidine
- Hydrofuran
- NCI-C60560
- NSC 57858
- Rcra waste number U213
- THF
- THF (tetrahydrofuran)
- Tetrahydrofuraan
- Tetrahydrofurane
- Tetrahydrofuranne
- Tetraidrofurano
- UN 2056
- oxacyclopentane
- oxolane
- tetramethylene oxide
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°gas : Standard gas enthalpy of combustion (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- εr : Dielectric Constant (Relative permittivity).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- pKa : Log10 of Acid Dissociation Constant.
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil(P) : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Vm : Molar Volume (m3/mol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2170; 0.2250] |
|
|
| ω | 0.2170 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2250 | ChemSep v8.3 pure component data Compiled value | |
| PAff | 822.10 | kJ/mol | NIST |
| Tig | 594.15 | K | NCMS SOLV-DB |
| BasG | 794.70 | kJ/mol | NIST |
| ΔcH°gas | -2533.20 ± 0.67 | kJ/mol | NIST |
| ΔcH°liquid | [-2505.80; -2501.20] | kJ/mol |
|
| ΔcH°liquid | -2505.80 ± 2.10 | kJ/mol | NIST |
| ΔcH°liquid | -2501.20 ± 0.84 | kJ/mol | NIST |
| μ | 1.63 | debye | ChemSep v8.3 pure component data Compiled value |
| η | 0.0004750 | Pa×s | A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents |
| εr | 7.58 | NCMS SOLV-DB | |
| Tflash,cc | 259.15 | K | NCMS SOLV-DB |
| ΔfG° | -79.69 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-184.20; -184.18] | kJ/mol |
|
| ΔfH°gas | -184.18 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -184.20 ± 0.71 | kJ/mol | NIST |
| ΔfusH° | 6.96 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [32.00; 32.90] | kJ/mol |
|
| ΔvapH° | 32.01 | kJ/mol | NCMS SOLV-DB |
| ΔvapH° | 32.16 | kJ/mol | NIST |
| ΔvapH° | 32.00 | kJ/mol | NIST |
| ΔvapH° | 32.90 | kJ/mol | NIST |
| ΔvapH° | 32.00 | kJ/mol | NIST |
| IE | [9.38; 9.74] | eV |
|
| IE | 9.40 ± 0.02 | eV | NIST |
| IE | 9.38 ± 0.05 | eV | NIST |
| IE | 9.38 | eV | NIST |
| IE | 9.41 | eV | NIST |
| IE | 9.42 ± 0.01 | eV | NIST |
| IE | 9.54 | eV | NIST |
| IE | 9.74 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.65 | eV | NIST |
| IE | 9.53 | eV | NIST |
| IE | 9.57 ± 0.02 | eV | NIST |
| log10WS | 0.49 | Estimated Solubility | |
| logPoct/wat | 0.460 | NCMS SOLV-DB | |
| McVol | 62.230 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | NCMS SOLV-DB | |
| NFPA Health | 2 | NCMS SOLV-DB | |
| NFPA Safety | 1 | NCMS SOLV-DB | |
| Pc | [5187.84; 5190.00] | kPa |
|
| Pc | 5190.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 5187.84 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 5190.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 5190.00 ± 50.66 | kPa | NIST |
| pKa | -2.08 | NCMS SOLV-DB | |
| Ptriple | 1.96e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [608.00; 640.00] |
|
|
| Inp | 609.90 | NIST | |
| Inp | 609.80 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 630.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 612.90 | NIST | |
| Inp | 623.20 | NIST | |
| Inp | 640.00 | NIST | |
| Inp | 640.00 | NIST | |
| Inp | 631.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | 632.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 630.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 633.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 636.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 638.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 627.00 | NIST | |
| Inp | 638.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 622.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 638.00 | NIST | |
| Inp | 632.00 | NIST | |
| Ip | [829.00; 915.00] |
|
|
| Ip | 868.00 | NIST | |
| Ip | 895.00 | NIST | |
| Ip | 888.00 | NIST | |
| Ip | 907.00 | NIST | |
| Ip | 915.00 | NIST | |
| Ip | 900.00 | NIST | |
| Ip | 903.00 | NIST | |
| Ip | 868.00 | NIST | |
| Ip | 861.00 | NIST | |
| Ip | 866.00 | NIST | |
| Ip | 867.00 | NIST | |
| Ip | 854.00 | NIST | |
| Ip | 857.00 | NIST | |
| Ip | 887.00 | NIST | |
| Ip | 829.00 | NIST | |
| Ip | 854.00 | NIST | |
| Ip | 898.00 | NIST | |
| Ip | 872.00 | NIST | |
| Ip | 868.00 | NIST | |
| Ip | 900.00 | NIST | |
| Ip | 829.00 | NIST | |
| S°gas | 301.70 ± 1.70 | J/mol×K | NIST |
| S°liquid | [203.80; 203.90] | J/mol×K |
|
| S°liquid | 203.80 | J/mol×K | NIST |
| S°liquid | 203.90 | J/mol×K | NIST |
| S°liquid | 203.90 | J/mol×K | NIST |
| Tboil | [330.15; 340.20] | K |
|
| Tboil | 339.12 | K | Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling |
| Tboil | 338.65 | K | Measurement and correlation of isobaric vapor-liquid equilibria of methanol + tetrahydrofuran + 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at 101.3 kPa |
| Tboil | 339.12 | K | Isobaric Vapor-Liquid Equilibrium for Binary System of Tetrahydrofuran + 1,4-Butanediol and gamma-Butyrolactone at 50.0 and 70.0 kPa |
| Tboil | 339.20 | K | Experimental Isobaric Vapor-Liquid Equilibrium Data for Binary Mixtures of Cyclic Ethers with (1-Methylethyl)benzene |
| Tboil | 339.12 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 339.12 | K | NCMS SOLV-DB |
| Tboil | 338.90 | K | NIST |
| Tboil | 339.15 ± 0.10 | K | NIST |
| Tboil | 339.05 ± 0.30 | K | NIST |
| Tboil | 339.20 ± 0.50 | K | NIST |
| Tboil | 340.20 | K | NIST |
| Tboil | 339.10 | K | NIST |
| Tboil | 338.90 ± 0.15 | K | NIST |
| Tboil | 339.35 ± 0.50 | K | NIST |
| Tboil | 337.90 ± 0.50 | K | NIST |
| Tboil | 339.00 ± 2.00 | K | NIST |
| Tboil | 340.00 ± 2.00 | K | NIST |
| Tboil | 339.10 ± 0.20 | K | NIST |
| Tboil | 339.65 ± 0.30 | K | NIST |
| Tboil | 337.65 ± 2.00 | K | NIST |
| Tboil | 337.65 ± 2.00 | K | NIST |
| Tboil | Outlier 330.15 ± 2.00 | K | NIST |
| Tboil | 340.15 ± 2.00 | K | NIST |
| Tc | [540.10; 541.00] | K |
|
| Tc | 540.50 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 540.20 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 540.20 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 540.20 | K | NIST |
| Tc | 540.10 ± 0.30 | K | NIST |
| Tc | Outlier 541.00 ± 1.50 | K | NIST |
| Tfus | [164.05; 165.15] | K |
|
| Tfus | 165.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 164.65 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 164.76 | K | NCMS SOLV-DB |
| Tfus | 165.10 ± 0.50 | K | NIST |
| Tfus | 164.15 ± 1.00 | K | NIST |
| Tfus | 164.63 ± 0.20 | K | NIST |
| Tfus | 164.05 ± 0.40 | K | NIST |
| Ttriple | [164.65; 164.76] | K |
|
| Ttriple | 164.65 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 164.76 ± 0.05 | K | NIST |
| Ttriple | 164.76 ± 0.02 | K | NIST |
| Ttriple | 164.76 ± 0.02 | K | NIST |
| Ttriple | 164.76 ± 0.02 | K | NIST |
| UQi | 2.40 | ChemSep v8.3 pure component data Compiled value | |
| URi | 2.94 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.224; 0.225] | m3/kmol |
|
| Vc | 0.224 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Vc | 0.224 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.224 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.225 ± 0.003 | m3/kmol | NIST |
| Vm | [8.17e-05; 8.17e-05] | m3/mol |
|
| Vm | 8.17e-05 | m3/mol | Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K |
| Vm | 8.17e-05 | m3/mol | Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K |
| Zc | [0.2590000; 0.2590000] |
|
|
| Zc | 0.2590000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value | |
| Zc | 0.2590000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil(P) | 339.15 | K | 96.60 | Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 333.20 | 10200.00 | 0.0004 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0003 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 85.90 | 298.15 | 882.02 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [44.72; 255.84] | J/mol×K | [150.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.16160e+01 | |||
| Coefficient B | -7.44850e+02 | |||
| Coefficient C | 6.14024e+00 | |||
| Coefficient D | -2.96160e-04 | |||
| Coefficient E | 7.44860e-08 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 44.72 | J/mol×K | 150.00 | Calculated Property |
| Cp,gas | 77.32 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 120.41 | J/mol×K | 450.00 | Calculated Property |
| Cp,gas | 156.96 | J/mol×K | 600.00 | Calculated Property |
| Cp,gas | 185.20 | J/mol×K | 750.00 | Calculated Property |
| Cp,gas | 206.69 | J/mol×K | 900.00 | Calculated Property |
| Cp,gas | 223.25 | J/mol×K | 1050.00 | Calculated Property |
| Cp,gas | 236.31 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 246.91 | J/mol×K | 1350.00 | Calculated Property |
| Cp,gas | 255.84 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [107.43; 135.79] | J/mol×K | [164.65; 339.12] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 8.33510e+01 | |||
| Coefficient B | 7.74140e+02 | |||
| Coefficient C | -6.52503e+00 | |||
| Coefficient D | 3.62550e-02 | |||
| Coefficient E | -3.55900e-05 | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 339.12 | |||
| Cp,liquid | 107.43 | J/mol×K | 164.65 | Calculated Property |
| Cp,liquid | 106.65 | J/mol×K | 184.04 | Calculated Property |
| Cp,liquid | 107.47 | J/mol×K | 203.42 | Calculated Property |
| Cp,liquid | 109.41 | J/mol×K | 222.81 | Calculated Property |
| Cp,liquid | 112.27 | J/mol×K | 242.19 | Calculated Property |
| Cp,liquid | 115.90 | J/mol×K | 261.58 | Calculated Property |
| Cp,liquid | 120.21 | J/mol×K | 280.96 | Calculated Property |
| Cp,liquid | 125.07 | J/mol×K | 300.35 | Calculated Property |
| Cp,liquid | 130.33 | J/mol×K | 319.73 | Calculated Property |
| Cp,liquid | 135.79 | J/mol×K | 339.12 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0055165; 0.0001696] | Pa×s | [164.65; 440.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.00470e+01 | |||
| Coefficient B | 8.96610e+02 | |||
| Coefficient C | -1.18640e-01 | |||
| Coefficient D | 2.56250e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 440.00 | |||
| η | 0.0055165 | Pa×s | 164.65 | Calculated Property |
| η | 0.0023095 | Pa×s | 195.24 | Calculated Property |
| η | 0.0012226 | Pa×s | 225.84 | Calculated Property |
| η | 0.0007528 | Pa×s | 256.43 | Calculated Property |
| η | 0.0005139 | Pa×s | 287.03 | Calculated Property |
| η | 0.0003776 | Pa×s | 317.62 | Calculated Property |
| η | 0.0002930 | Pa×s | 348.22 | Calculated Property |
| η | 0.0002369 | Pa×s | 378.81 | Calculated Property |
| η | 0.0001979 | Pa×s | 409.41 | Calculated Property |
| η | 0.0001696 | Pa×s | 440.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [37.90; 0.66] | kJ/mol | [164.65; 540.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 4.77063e+01 | |||
| Coefficient B | 8.30300e-01 | |||
| Coefficient C | -6.17577e-01 | |||
| Coefficient D | -2.53996e-01 | |||
| Coefficient E | 5.01899e-01 | |||
| Critical temperature, Tc (K) | 5.40200e+02 | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 540.15 | |||
| ΔvapH | 37.90 | kJ/mol | 164.65 | Calculated Property |
| ΔvapH | 35.99 | kJ/mol | 206.37 | Calculated Property |
| ΔvapH | 34.19 | kJ/mol | 248.09 | Calculated Property |
| ΔvapH | 32.39 | kJ/mol | 289.82 | Calculated Property |
| ΔvapH | 30.46 | kJ/mol | 331.54 | Calculated Property |
| ΔvapH | 28.19 | kJ/mol | 373.26 | Calculated Property |
| ΔvapH | 25.31 | kJ/mol | 414.98 | Calculated Property |
| ΔvapH | 21.38 | kJ/mol | 456.71 | Calculated Property |
| ΔvapH | 15.53 | kJ/mol | 498.43 | Calculated Property |
| ΔvapH | 0.66 | kJ/mol | 540.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.37e-04; 5167.31] | kPa | [164.65; 540.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.58357e+01 | |||
| Coefficient B | -6.23655e+03 | |||
| Coefficient C | -9.22114e+00 | |||
| Coefficient D | 7.80890e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 540.15 | |||
| Pvap | 1.37e-04 | kPa | 164.65 | Calculated Property |
| Pvap | 0.04 | kPa | 206.37 | Calculated Property |
| Pvap | 1.40 | kPa | 248.09 | Calculated Property |
| Pvap | 14.82 | kPa | 289.82 | Calculated Property |
| Pvap | 78.73 | kPa | 331.54 | Calculated Property |
| Pvap | 271.85 | kPa | 373.26 | Calculated Property |
| Pvap | 709.70 | kPa | 414.98 | Calculated Property |
| Pvap | 1538.20 | kPa | 456.71 | Calculated Property |
| Pvap | 2941.04 | kPa | 498.43 | Calculated Property |
| Pvap | 5167.31 | kPa | 540.15 | Calculated Property |
| Pvap | [1.27e-04; 5170.61] | kPa | [164.65; 540.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.83577e+01 | |||
| Coefficient B | -6.33998e+03 | |||
| Coefficient C | -9.60880e+00 | |||
| Coefficient D | 8.18348e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 540.15 | |||
| Pvap | 1.27e-04 | kPa | 164.65 | Calculated Property |
| Pvap | 0.04 | kPa | 206.37 | Calculated Property |
| Pvap | 1.38 | kPa | 248.09 | Calculated Property |
| Pvap | 14.80 | kPa | 289.82 | Calculated Property |
| Pvap | 78.83 | kPa | 331.54 | Calculated Property |
| Pvap | 272.18 | kPa | 373.26 | Calculated Property |
| Pvap | 709.91 | kPa | 414.98 | Calculated Property |
| Pvap | 1537.51 | kPa | 456.71 | Calculated Property |
| Pvap | 2939.69 | kPa | 498.43 | Calculated Property |
| Pvap | 5170.61 | kPa | 540.15 | Calculated Property |
| Pvap | [19.92; 269.76] | kPa | [296.29; 372.80] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40945e+01 | |||
| Coefficient B | -2.76988e+03 | |||
| Coefficient C | -4.68180e+01 | |||
| Reference | Scott D.W., 1970 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 296.29 | |||
| Temperature range, max. | 372.80 | |||
| Pvap | 19.92 | kPa | 296.29 | Calculated Property |
| Pvap | 28.72 | kPa | 304.79 | Calculated Property |
| Pvap | 40.45 | kPa | 313.29 | Calculated Property |
| Pvap | 55.78 | kPa | 321.79 | Calculated Property |
| Pvap | 75.45 | kPa | 330.29 | Calculated Property |
| Pvap | 100.28 | kPa | 338.80 | Calculated Property |
| Pvap | 131.15 | kPa | 347.30 | Calculated Property |
| Pvap | 169.01 | kPa | 355.80 | Calculated Property |
| Pvap | 214.86 | kPa | 364.30 | Calculated Property |
| Pvap | 269.76 | kPa | 372.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1010.35; 330.34] | kg/m3 | [164.65; 540.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 7.59994e+01 | |||
| Coefficient B | 2.57540e-01 | |||
| Coefficient C | 5.40200e+02 | |||
| Coefficient D | 2.67760e-01 | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 540.15 | |||
| ρl | 1010.35 | kg/m3 | 164.65 | Calculated Property |
| ρl | 972.48 | kg/m3 | 206.37 | Calculated Property |
| ρl | 932.60 | kg/m3 | 248.09 | Calculated Property |
| ρl | 890.21 | kg/m3 | 289.82 | Calculated Property |
| ρl | 844.59 | kg/m3 | 331.54 | Calculated Property |
| ρl | 794.64 | kg/m3 | 373.26 | Calculated Property |
| ρl | 738.39 | kg/m3 | 414.98 | Calculated Property |
| ρl | 671.93 | kg/m3 | 456.71 | Calculated Property |
| ρl | 584.57 | kg/m3 | 498.43 | Calculated Property |
| ρl | 330.34 | kg/m3 | 540.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 2.81e-05] | N/m | [164.65; 535.64] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -3.68860e-02 | |||
| Coefficient B | 4.45000e+00 | |||
| Coefficient C | -2.34120e+00 | |||
| Coefficient D | -9.81780e-04 | |||
| Coefficient E | -1.53490e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 540.15 K. | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 535.64 | |||
| γ | 0.04 | N/m | 164.65 | Calculated Property |
| γ | 0.04 | N/m | 205.87 | Calculated Property |
| γ | 0.03 | N/m | 247.09 | Calculated Property |
| γ | 0.03 | N/m | 288.31 | Calculated Property |
| γ | 0.02 | N/m | 329.54 | Calculated Property |
| γ | 0.02 | N/m | 370.76 | Calculated Property |
| γ | 0.01 | N/m | 411.98 | Calculated Property |
| γ | 0.01 | N/m | 453.20 | Calculated Property |
| γ | 0.00 | N/m | 494.42 | Calculated Property |
| γ | 2.81e-05 | N/m | 535.64 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.13] | W/m×K | [164.65; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.04390e-05 | |||
| Coefficient B | 1.44820e+00 | |||
| Coefficient C | 7.29360e+02 | |||
| Coefficient D | -9.82930e+03 | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 164.65 | Calculated Property |
| λgas | 0.01 | W/m×K | 257.47 | Calculated Property |
| λgas | 0.02 | W/m×K | 350.28 | Calculated Property |
| λgas | 0.03 | W/m×K | 443.10 | Calculated Property |
| λgas | 0.04 | W/m×K | 535.92 | Calculated Property |
| λgas | 0.06 | W/m×K | 628.73 | Calculated Property |
| λgas | 0.07 | W/m×K | 721.55 | Calculated Property |
| λgas | 0.09 | W/m×K | 814.37 | Calculated Property |
| λgas | 0.11 | W/m×K | 907.18 | Calculated Property |
| λgas | 0.13 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.09] | W/m×K | [164.65; 433.56] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -2.20850e-01 | |||
| Coefficient B | 9.59710e+00 | |||
| Coefficient C | -9.94960e-01 | |||
| Coefficient D | -1.74150e-04 | |||
| Coefficient E | -6.49580e-07 | |||
| Temperature range, min. | 164.65 | |||
| Temperature range, max. | 433.56 | |||
| λliquid | 0.15 | W/m×K | 164.65 | Calculated Property |
| λliquid | 0.15 | W/m×K | 194.53 | Calculated Property |
| λliquid | 0.14 | W/m×K | 224.41 | Calculated Property |
| λliquid | 0.13 | W/m×K | 254.29 | Calculated Property |
| λliquid | 0.12 | W/m×K | 284.17 | Calculated Property |
| λliquid | 0.12 | W/m×K | 314.04 | Calculated Property |
| λliquid | 0.11 | W/m×K | 343.92 | Calculated Property |
| λliquid | 0.10 | W/m×K | 373.80 | Calculated Property |
| λliquid | 0.10 | W/m×K | 403.68 | Calculated Property |
| λliquid | 0.09 | W/m×K | 433.56 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetrahydrofuran.
Mixtures
- Acetonitrile + Tetrahydrofuran
- Acetone + Tetrahydrofuran
- 1,2-Ethanediol + Tetrahydrofuran + Methyl Alcohol
- 1,2-Ethanediol + Tetrahydrofuran
- Ethanol + Tetrahydrofuran + Cyclohexane
- Ethanol + Tetrahydrofuran
- Ethyl ether + Tetrahydrofuran
- Ethyl Acetate + Tetrahydrofuran + Cyclohexane
- Ethyl Acetate + Tetrahydrofuran
- Benzene + Tetrahydrofuran
- 1-Butanol + Tetrahydrofuran
- Trichloromethane + Tetrahydrofuran + Cyclohexane
- Trichloromethane + Tetrahydrofuran
- Tetrahydrofuran + Cyclohexane
- Tetrahydrofuran + Cyclohexane + Water
- Acetic acid + Tetrahydrofuran
- n-Hexane + Tetrahydrofuran
- n-Hexane + Tetrahydrofuran + Water
- 2-Propanol + Tetrahydrofuran
- 1-Hexene + Tetrahydrofuran
Find more mixtures with Tetrahydrofuran.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
- Volumetric Properties of the Ionic Liquid, 1-Butyl-3-methylimidazolium Tetrafluoroborate, in Organic Solvents at T = 298.15 K
- A Digital Variable-Angle Rolling-Ball Viscometer for Measurement of Viscosity, Density, and Bubble-Point Pressure of CO2 and Organic Liquid Mixtures
- Viscosity Behavior of Some Oxygen Containing Compounds
- Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
- (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure
- Measurement and correlation of vapor liquid equilibria of binary systems containing the ionic liquids [EMIM][(CF3SO2)2N], [BMIM][(CF3SO2)2N], [MMIM][(CH3)2PO4] and oxygenated organic compounds respectively water
- Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
- Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1) + 1-chlorobutane (2) + 2-butanol (3) at 283.15, 298.15 and 313.15 K
- Measurement of heat capacities of ionic liquids by differential scanning calorimetry
- Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
- Liquid liquid equilibria and partitioning in organic aqueous systems
- Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
- 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
- Temperature dependence of limiting activity coefficients and Henry s law constants of cyclic and open-chain ethers in water
- Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
- Phase equilibrium and thermophysical properties of mixtures containing a cyclic ether and 1-chloropropane
- High-pressure vapor-liquid equilibria for carbon dioxide + tetrahydrofuran mixtures
- Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Densities and ultrasonic studies for binary mixtures of tetrahydrofuran with chlorobenzenes, chlorotoluenes and nitrotoluenes at 298.15 K
- Solubility of citric, malonic, and malic acids in different solvents from 303.2 to 333.2 K
- Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
- Conductivity is a contrivance to explore ion-pair and triple-ion structure of ethanoates in tetrahydrofuran, dimethyl sulfoxide and their binaries
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
- Effect of solvent on the volumetric behavior ofN,N' -salicylidenephenyl diamine (Salophen) Schiff base at differenttemperatures (288.15 - 318.15) K
- Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
- Excess Gibbs energies and volumes of the ternary system ethanol + dimethylformamide + tetrahydrofuran at 298.15K
- Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
- Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
- Vapor-Liquid Equilibrium for Tetrahydrofuran + Methanol + Tetrafluoroborate-based ionic liquids at 101.3 kPa
- Experiments on the continuous separation of gas mixtures via dissolution and hydrate formation in the presence of THF
- Thermodynamic models for determination of the solubility of 2, 5-bis(2-furylmethylidene) cyclopentan-1-one in different solvents at temperatures ranging from 308.15 to 403.15 K.
- Vapor-liquid equilibria for tetrahydrofuran + ethanol system containing three different ionic liquids at 101.3 kPa
- Volumetric and viscometric behavior of the binary systems ethyl lactate + 1,2- propanediol, + 1,3-propanediol, + tetrahydrofuran and + tetraethylene glycol dimethyl ether. New UNIFAC-VISCO and ASOG-VISCO parameters determination
- Thermostabilities and solubilities of flame retardant bisphenol S-bis (5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy phosphate ester) as a function of temperature
- (Liquid + liquid) equilibria in the (water + tetrahydrofuran + methylcyclohexane) ternary system at temperatures between (278 and 343) K and atmospheric pressure: Experimental data and correlation
- Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- Measurement and correlation of isobaric vapor-liquid equilibria of methanol + tetrahydrofuran + 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at 101.3 kPa
- Partitioning of diuron in a novel aqueous two-phase system based on polyols and tetrahydrofuran
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- Novel phase diagrams of aqueous two-phase systems based on tetrahydrofuran + carbohydrates + water: equilibrium data and partitioning experiments
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Guaiacol and its mixtures: new data and predictive models Part 2: Gibbs energy of solvation
- Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Unravelling various types of non-covalent interactions of benzyl amine with ethers in n-hexane at 303.15 K by ultrasonic and DFT methods
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Salt effect on liquid-liquid equilibria of tetrahydrofuran/water/5-hydroxymethylfurfural systems
- Standard partial molar volumes of some electrolytes in ethylene carbonate based mixtures
- Excess molar enthalpies of the ternary mixtures: {tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-dodecane} at the temperature 298.15 K
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- Tailor-made ionic liquids
- Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
- Phase equilibria for ternary liquid systems of (water + tetrahydrofuran + nonprotic aromatic solvent) at T = 298.2 K
- Excess molar enthalpies of the ternary mixtures: (tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether + n-octane) at the temperature 298.15 K
- Volumetric and compressibility behaviour of ionic liquid, 1-n-butyl-3-methylimidazolium hexafluorophosphate and tetrabutylammonium hexafluorophosphate in organic solvents at T = 298.15 K
- Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.
- Isothermal compressibility and internal pressure studies of some non-electrolytes in aqueous solutions at low temperatures
- Apparent molar volumes and apparent molar heat capacities of aqueous tetrahydrofuran, dimethyl sulfoxide, 1,4-dioxane, and 1,2-dimethoxyethane at temperatures from 278.15 K to 393.15 K and at the pressure 0.35 MPa
- Volumetric properties of binary mixtures of ethers and acetonitrile: Experimental results and application of the Prigogine Flory Patterson theory
- Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
- Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
- Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Volumetric properties of the (tetrahydrofuran + water) and (tetra-n-butyl ammonium bromide + water) systems: Experimental measurements and correlations
- Partial molar volumes of organic solutes in water. XXI: Cyclic ethers at temperatures T = (278 to 373) K and at low pressure
- Partial molar volumes of organic solutes in water. XXII. Cyclic ethers at temperatures (298 to 573) K and pressures up to 30 MPa
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Excess molar volume, viscosity, and refractive index study for the ternary mixture {2-methyl-2-butanol (1) + tetrahydrofuran (2) + propylamine (3)} at different temperatures. Application of the ERAS-model and Peng Robinson Stryjek Vera equation of state
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Phenomenon of "negative partial molar expansibility" of water in tetrahydrofuran: How plausible is it? Discussion on the paper "Volumetric properties on the (tetrahydrofuran + water) and (tetra-n-butylammonium bromide + water) systems: Experimental measurements and correlations" by Veronica Belandria, Ammir H. Mohammadi and Dominique Richon [J. Chem. Thermodyn. 41 (2009) 1382 1386]
- Excess molar enthalpies of ternary mixtures (1-hexene + tetrahydrofuran + 2,2-dimethylbutane or 2,3-dimethylbutane) at the temperature 298.15 K
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- Vapor pressures and activity coefficients of binary mixtures of 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide with acetonitrile and tetrahydrofuran
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- The potential of head-space gas chromatography for VLE measurements
- Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
- Clarification of the volumetric properties of the (tetrahydrofuran + water) systems [J. Chem. Thermodyn. 41 (2009) 1382 1386]: Author s statement
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Thermodynamic surface properties of [BMIm][NTf2] or [EMIm][NTf2] binary mixtures with tetrahydrofuran, acetonitrile or dimethylsulfoxide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Solubility and solution thermodynamics of 2,3,4,5-tetrabromothiophene in (ethanol + tetrahydrofuran) binary solvent mixtures
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Experimental and theoretical excess molar properties of imidazolium based ionic liquids with molecular organic solvents I. 1-Hexyl-3- methylimidazlouim tetraflouroborate and 1-octyl-3-methylimidazlouim tetraflouroborate with cyclic ethers
- To the issue of temperature-dependent behavior of standard molar volumes of components in the binary system (water + tetrahydrofuran) at ambient pressure
- Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- (Liquid + liquid), (solid + liquid), and (solid + liquid + liquid) equilibria of systems containing cyclic ether (tetrahydrofuran or 1,3-dioxolane), water, and a biological buffer MOPS
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Investigation on thermophysical and excess properties of binary mixtures of imidazolium based ionic liquids at temperatures (293.15 to 323.15) K: III [Cnmim][PF6] (n = 4, 6, 8) + THF
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Measurement and correlation of the solubility of rivaroxaban (form I) in binary mixtures of ethyl acetate with tetrahydrofuran, N,N-dimethylformamide, and N,N-dimethylacetamide from T = (278.15 to 318.15) K
- Thermodynamic models for determination of the solubility of omeprazole in pure and mixture organic solvents from T = (278.15 to 333.15) K
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamic models for determination of the solubility of 4-(4-aminophenyl)-3-morpholinone in different pure solvents and (1,4-dioxane + ethyl acetate) binary mixtures with temperatures from (278.15 to 333.15) K
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
- Densities, ultrasonic speeds and refractive indices of phenetole with N-methyl-2-pyrrolidone, N,N-dimethylformamide and tetrahydrofuran binary mixtures at different temperatures
- Determination and correlation thermodynamic models for solid liquid equilibrium of the Nifedipine in pure and mixture organic solvents
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Solubility of oxcarbazepine in eight solvents within the temperature range T = (288.15 308.15) K
- Measurement and correlation of solubility of succinic anhydride in pure solvents and binary solvent mixtures
- Temperature and concentration dependence of volumetric properties of (tetrahydrofuran + methyl acrylate, or + ethyl acrylate, or + n-butyl acrylate, or + tert-butyl acrylate) binary mixtures
- Thermodynamic models for determination of solid liquid equilibrium of the 6-benzyladenine in pure and binary organic solvents
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Thermodynamic models for determination of the solid-liquid equilibrium of istradefylline in ethyl acetate plus (isopropanol, tetrahydrofuran, acetone) binary solvent mixtures
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- Benchmark properties of pyrazole derivatives as a potential liquid organic hydrogen carrier: Evaluation of thermochemical data with complementary experimental and computational methods
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
- Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
- Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
- Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents: IV. Alkylamines in 1,4-dioxane and oxolane at 303.15K
- Thermodynamic and acoustic properties of binary mixtures of oxolane with aniline and substituted anilines at 303.15, 313.15 and 323.15 K
- Water as a solute in aprotic dipolar solvents. 1. D2O-H2O solute isotope effects on the enthalpy of water dissolution in acetone, tetrahydrofuran and 1,4-dioxane at 298.15 K
- Thermodynamic and acoustic properties of binary mixtures of ethers. III. Diisopropyl ether or oxolane with o- or m-toluidines at 303.15, 313.15 and 323.15 K
- Thermodynamic and acoustic properties of binary mixtures of ethers. IV. Diisopropyl ether or oxolane with N,N-dimethylaniline or N,Ndiethylaniline at 303.15, 313.15 and 323.15 K
- Thermodynamic and acoustic properties of binary mixtures of ethers. V. Diisopropyl ether or oxolane with 2- or 3-chloroanilines at 303.15, 313.15 and 323.15 K
- Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
- Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Thermodynamic properties of betulinic acid in THF + water mixed solvents at different temperatures
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- Enthalpies of solution, enthalpies of fusion and enthalpies of solvation of polyaromatic hydrocarbons: Instruments for determination of sublimation enthalpy at 298.15 K
- Thermodynamics of hydrogen bonding and van der Waals interactions of organic solutes in solutions of imidazolium based ionic liquids: "structure-property" relationships
- Thermodynamic of dissolution and hydrogen bond of the pyrrole, N-methylpyrrole with proton acceptors
- Enthalpies of solution of 1-ethyl- and 1-butyl-3-methylimidazolium based ionic liquids in tetrahydrofuran and chloroform at 298.15 K: Thermochemical proton acceptor scale of anions
- Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
- Thermochemistry of hydrogen bonding of linear and cyclic amides inproton acceptors media
- Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
- Thermochemistry of hydrogen bonding of proton acceptors in the media of linear and cyclic amides. Cooperativity effects in multi-particle complexes of amides
- Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
- Thermodynamic Models for Determination of the Solubility of Boc-(R)-3-Amino-4-(2, 4, 5-trifluorophenyl)butanoic acid in Different Pure Solvents and (Tetrahydrofuran + n-Butanol) Binary Mixtures with Temperatures from 280.15 to 330.15 K
- Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
- Solubility Measurement and Correlation of (+)-Biotin Intermediate Lactone in Different Organic Solvents from (287.15 to 323.75) K
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
- Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
- Solubility and Thermodynamic Behavior of Veramoss in Different Pure Solvents and {Ethanol + Water} Mixtures from T = 283.15 to 333.15 K
- Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
- Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
- Phase Behavior of Binary Mixtures Containing Succinic Acid or Its Esters
- Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
- Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
- Solid-Liquid Phase Equilibrium and Thermodynamic Properties of Olaparib in Selected Organic Solvents and (Tetrahydrofuran + MTBE, Acetonitrile + Isopropyl Alcohol) Binary Solvent Mixtures
- Isobaric Vapor-Liquid Equilibrium for Binary System of Tetrahydrofuran + 1,4-Butanediol and gamma-Butyrolactone at 50.0 and 70.0 kPa
- Synthesis and Solubility of 5,5-Dimethyl-2-(phenyl(phenylamino)methyl)-1,3,2-dioxaphosphinane 2-oxide in Selected Solvents between 278.15 K and 347.15 K
- Determination and Thermodynamic Analysis of the Solubility of Limonin in Eight Organic Solvents and Ethyl Acetate + 2-Propanol Binary Solvents from 283.2 to 323.2 K
- Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
- Experimental Determination and Thermodynamic Models for Solid-Liquid Equilibrium of 4-(4-Aminophenoxy)-N-methylpyridine-2-carboxamide in Pure and Binary Solvent Mixtures for T = (278.15-328.15) K
- Measurement and Correlation of the Solubility of 5-Fluorouracil in Pure and Binary Solvents
- Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
- Solubility Measurements at 296 and 310 K and Physicochemical Characterization of Abiraterone and Abiraterone Acetate
- Measurement and Correlation of the Solubility of Mifepristone in Eight Pure and Water + Methanol Mixed Solvents at Temperatures from 273.15 to 318.15 K
- Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
- Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
- Solubility Measurement, Correlation, and Molecular Interactions of 3-Methyl-6-nitroindazole in Different Neat Solvents and Mixed Solvents from T = 278.15 to 328.15 K
- Solubility Study of (2E)-1-(3-Pyridyl)-3-(dimethylamino)-2-propen-1-one in Different Pure Solvents and Binary Solvent Mixtures from 278.15 to 328.15 K
- Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
- Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
- Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
- Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
- Solubility Measurement and Modeling of 3-Hydroxy-2-nitropyridine in Ten Pure Solvents and Two Binary Mixed Solvents for T = (278.15-318.15) K
- Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
- Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
- Excess Enthalpies of the Ternary Mixtures: Tetrahydrofuran + (Hexane or Cyclohexane) + Decane at 298.15K
- Vapor-Liquid Equilibria of the Binary Carbon Dioxide-Tetrahydrofuran Mixture System
- Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
- Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
- Thermodynamic Properties of Water + Tetrahydrofuran and Water + 1,4-Dioxane Mixtures at (303.15, 313.15, and 323.15) K
- Partition Coefficients of Organic Solutes between Supercritical Carbon Dioxide and Water: Experimental Measurements and Empirical Correlations
- Excess Enthalpy, Excess Volume, Viscosity Deviation, and Speed of Sound Deviation for the Mixture Tetrahydrofuran + 2,2,2-Trifluoroethanol at (283.15, 298.15, and 313.15) K
- Double Azeotropy in Binary Mixtures 1,1,1,2,3,4,4,5,5,5-Decafluoropentane High-Boiling Diastereomer + Tetrahydrofuran
- Solubilities of Bis (2,2,6,6-Tetramethyl-4-Piperidinyl) Maleate in Hexane, Heptane, Octane, m-Xylene and Tetrahydrofuran from (253.15 to 310.15) K
- Influence of Ionic Liquids on the Phase Behavior of Aqueous Azeotropic Systems
- Excess Molar volumes and Surface Tensions of Trimethylbenzene with Tetrahydrofuran Tetrachloromethane and Dimethylsulfoxide at 298.15 K
- Liquid-Liquid Equilibria for the Ternary Systems of (Water + Tetrahydrofuran + Polar Solvent) at 298.15 K
- High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
- Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
- Study of the Surface Tension of Chlorocyclohexane or Bromocyclohexane with Some Cyclic Ethers
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- Solubility of Organic Systems Containing 1,4-Dioxan-2-one
- Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
- Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
- Densities, Viscosities, and Sound Speeds of Some Acetate Salts in Binary Mixtures of Tetrahydrofuran and Methanol at (303.15, 313.15, and 323.15) K
- Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
- Solubility of 4-(3,4-Dichlorophenyl)-1-tetralone in Some Organic Solvents
- Solubility of 3-Nitrophthalic Acid in Different Solvents between 278 K and 353 K
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Solubility of Sulpiride in Pure Organic Solvents between (278 and 333) K
- Volumetric Properties of Binary Mixtures Containing Ionic Liquids and Some Aprotic Solvents
- Solubility of Decabromodiphenyl Ether in Different Solvents at (283.0 to 323.0) K
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
- Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
- Solubility of Florfenicol in Different Solvents at Temperatures from (278 to 318) K
- Solubilities of (a,Z)-2-Amino-a-(methoxyimino)-4-thiazoleethanethioic Acid S-2-Benzothiazolyl Ester in Different Pure Solvents and Binary Mixtures of Tetrahydrofuran + Dichloromethane or 1,2-Dichloroethane
- Excess Molar Enthalpies of Dipropyl Ether + Dibutyl Ether + (1-Hexene or Tetrahydrofuran) at 298.15 K
- Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Surface Tensions and the Gibbs Excess Surface Concentration of Binary Mixtures of the Ionic Liquid 1-Ethyl-3-methylimidazolium Bis[(trifluoromethyl)sulfonyl]imide with Tetrahydrofuran and Acetonitrile
- Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
- Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
- Ultrasonic and Volumetric Properties of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with 2-Propanol or Tetrahydrofuran at Several Temperatures
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Antisolvent Precipitation of Vitamin B6: A Thermodynamic Study
- Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
- Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
- Partial Molar Isentropic Compressions of Selected Cyclic Ethers at Infinite Dilution in Water at Temperatures T = (278 to 318) K and Atmospheric Pressure
- Liquid Liquid Equilibria for the Ternary Systems of Perfluorohexane or Perfluamine + Hydrofluoroether + Tetrahydrofuran at 298.15 K or 273.15 K
- Thermodynamic and Spectroscopic Study of the Ternary System Dimethyladipate + Tetrahydrofuran +1-Butanol at T = (288.15 to 323.15) K
- Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Vapor Liquid Equilibrium for Ternary and Binary Mixtures of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa
- Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
- Acoustic and Volumetric Properties of Binary Mixtures of Ionic Liquid 1-Butyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide with Acetonitrile and Tetrahydrofuran
- Thermodynamics of Fluconazole Solubility in Various Solvents at Different Temperatures
- Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
- Determination and Correlation of Solubilities of Lithium Bis(oxalate)borate in Six Different Solvents from (293.15 to 363.15) K
- 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
- Solubility and Thermodynamic Functions of Isatin in Pure Solvents
- Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
- Liquid-Liquid Equilibrium for the Quaternary System Water + Tetrahydrofuran + Toluene + 1-Butanol Mixture at 25 deg C and Atmospheric Pressure
- Solubility of Irbesartan (Form A) in Different Solvents between 278 K and 323 K
- Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
- Thermodynamics of Mixing Tetrahydrofuran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
- Viscosity, Density, Speed of Sound, and Refractive Index of Binary Mixtures of Organic Solvent + Ionic Liquid, 1-Butyl-3-methylimidazolium Hexafluorophosphate at 298.15 K
- Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
- Ion-Pair and Triple-Ion Formation by Some Tetraalkylammonium Iodides in Binary Mixtures of 1,4-Dioxane + Tetrahydrofuran
- Solubility of Trimethoprim (TMP) in Different Organic Solvents from (278 to 333) K
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
- Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
- Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
- Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
- solubility of L-(+)-ascorbic acid in water, ethanol, methanol, propan-2-ol, acetone, acetonitrile, ethyl acetate, and tetrahydrofuran from (293 to 323) K
- Experimental Isobaric Vapor-Liquid Equilibrium Data for Binary Mixtures of Cyclic Ethers with (1-Methylethyl)benzene
- Solubility of Carbamazepine (Form III) in Different Solvents from (275 to 343) K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubility of Methane in Tetrahydrofuran + Ethanol at High Pressures
- Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
- Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
- Solubility of Chloroquine Diphosphate and 4,7-Dichloroquinoline in Water, Ethanol, Tetrahydrofuran, Acetonitrile, and Acetone from (298.2 to 333.2) K
- Solubilities of Terephthalic Acid, Phthalic Acid, and Isophthalic Acid in Tetrahydrofuran, Cyclohexanone, 1,2-Diethoxyethane, and Acetophenone
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
- Measurement and Correlation of Solubility of Pimelic Acid in Ether, Tetrahydrofuran, Ethanol, and Methanol
- Solubility of 5-Amino Salicylic Acid in Different Solvents at Various Temperatures
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Joback Method
- KDB
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
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