Chemical Properties of 1,4-Dioxane (CAS 123-91-1)

1,4-Dioxane

InChI
InChI=1S/C4H8O2/c1-2-6-4-3-5-1/h1-4H2
InChI Key
RYHBNJHYFVUHQT-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
C1COCCO1
Molecular Weight1
88.11
CAS
123-91-1
Other Names
  • 1,4-Diethylene dioxide
  • 1,4-Diethyleneoxide
  • 1,4-Dioxan
  • 1,4-Dioxin, tetrahydro-
  • 1,4-dioxacyclohexane
  • Di(ethylene oxide)
  • Diethylene dioxide
  • Diethylene ether
  • Diokan
  • Dioksan
  • Diossano-1,4
  • Dioxaan-1,4
  • Dioxan
  • Dioxan-1,4
  • Dioxane-1,4
  • Dioxanne
  • Dioxyethylene ether
  • Glycol ethylene ether
  • Glycol ethylene ether 8
  • NCI-C03689
  • NE 220
  • NSC 8728
  • Rcra waste number U108
  • Tetrahydro-p-dioxin
  • UN 1165
  • dioxane
  • p-Dioxan
  • p-Dioxin, tetrahydro-
  • p-dioxane
  • tetrahydro-1,4-dioxin
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Contents

  1. Physical Properties
  2. Temperature Dependent Properties
  3. Pressure Dependent Properties
  4. Datasets
  5. Correlations
  6. Similar Compounds
  7. Mixtures
  8. Sources

Physical Properties

Property Value Unit Source
ω [0.2793; 0.2880]   Show Hide
ω 0.2880 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.2793 ChemSep v8.3 pure component data Compiled value
ω 0.2810 KDB
PAff 797.40 kJ/mol NIST
Tig [453.15; 453.15] K Show Hide
Tig 453.15 K KDB
Tig 453.15 K NCMS SOLV-DB
BasG 770.00 kJ/mol NIST
ΔcH°liquid [-2363.90; -2186.80] kJ/mol Show Hide
ΔcH°liquid -2362.23 ± 0.99 kJ/mol NIST
ΔcH°liquid -2363.90 ± 0.50 kJ/mol NIST
ΔcH°liquid -2346.20 kJ/mol NIST
ΔcH°liquid -2186.80 kJ/mol NIST
μ [0.00; 0.40] debye Show Hide
μ 0.00 debye ChemSep v8.3 pure component data Compiled value
μ 0.40 debye KDB
η 0.0011960 Pa×s Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
εr 2.21 NCMS SOLV-DB
LFL 1.97 % in Air KDB
UFL 22.50 % in Air KDB
Tflash,cc [285.15; 296.48] K Show Hide
Tflash,cc 296.48 K KDB
Tflash,cc 285.15 K NCMS SOLV-DB
Tflash,oc 285.37 K KDB
ΔfG° [-181.60; -180.90] kJ/mol Show Hide
ΔfG° -181.60 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -180.90 kJ/mol KDB
Rg 3.1100 KDB
ΔfH°gas [-318.00; -315.30] kJ/mol Show Hide
ΔfH°gas -315.80 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -315.30 kJ/mol KDB
ΔfH°gas -315.30 ± 0.80 kJ/mol NIST
ΔfH°gas -318.00 ± 2.00 kJ/mol NIST
ΔfH°liquid [-355.13; -353.50] kJ/mol Show Hide
ΔfH°liquid -355.13 ± 0.86 kJ/mol NIST
ΔfH°liquid -353.50 ± 0.80 kJ/mol NIST
ΔfusH° 12.84 kJ/mol Joback Calculated Property
ΔvapH° [34.10; 39.80] kJ/mol Show Hide
ΔvapH° 35.56 kJ/mol NCMS SOLV-DB
ΔvapH° 38.66 kJ/mol NIST
ΔvapH° 38.64 ± 0.05 kJ/mol NIST
ΔvapH° 39.80 kJ/mol NIST
ΔvapH° 38.60 ± 0.10 kJ/mol NIST
ΔvapH° 35.50 kJ/mol NIST
ΔvapH° 34.10 kJ/mol NIST
ΔvapH° 37.49 kJ/mol NIST
IE [9.13; 9.43] eV Show Hide
IE 9.19 ± 0.01 eV NIST
IE 9.19 ± 0.01 eV NIST
IE 9.13 ± 0.03 eV NIST
IE 9.40 eV NIST
IE 9.43 eV NIST
IE 9.41 eV NIST
IE 9.30 ± 0.10 eV NIST
IE 9.43 eV NIST
log10WS 0.27 Relay (1.0) Calculated Property
logPoct/wat -0.270 NCMS SOLV-DB
McVol 68.100 ml/mol McGowan Calculated Property
NFPA Fire 3 NCMS SOLV-DB
NFPA Health 2 NCMS SOLV-DB
NFPA Safety 1 NCMS SOLV-DB
Pc [5000.00; 5471.55] kPa Show Hide
Pc 5210.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc 5208.11 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 5170.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 5210.00 kPa KDB
Pc Outlier 5471.55 ± 303.98 kPa NIST
Pc 5210.00 ± 68.94 kPa NIST
Pc 5000.00 ± 70.00 kPa NIST
pKa -2.92 NCMS SOLV-DB
Ptriple 2.53 kPa ChemSep v8.3 pure component data Compiled value
ρc 360.35 ± 9.69 kg/m3 NIST
Inp [643.00; 731.30]   Show Hide
Inp 670.10 NIST
Inp Outlier 648.00 NIST
Inp 690.00 NIST
Inp 669.70 NIST
Inp 671.00 NIST
Inp Outlier 731.30 NIST
Inp 718.00 NIST
Inp Outlier 643.00 NIST
Inp 705.00 NIST
Inp 721.00 NIST
Inp Outlier 648.00 NIST
Inp 687.00 NIST
Inp 702.00 NIST
Inp 660.30 NIST
Inp 680.00 NIST
Inp 697.00 NIST
Inp Outlier 651.00 NIST
Inp 687.00 NIST
Inp 690.00 NIST
Inp 696.00 NIST
Inp 696.00 NIST
Inp 698.00 NIST
Inp 694.00 NIST
Inp 690.00 NIST
Inp 692.00 NIST
Inp 693.00 NIST
Inp 696.00 NIST
Inp 699.00 NIST
Inp 690.00 NIST
Inp 696.00 NIST
Inp 696.00 NIST
Inp 697.00 NIST
Inp 680.00 NIST
Inp 694.00 NIST
Inp 694.00 NIST
Inp 705.00 NIST
Inp 690.00 NIST
Inp 702.00 NIST
Inp 690.00 NIST
Inp 696.00 NIST
Inp 706.00 NIST
Inp 692.00 NIST
Inp 686.00 NIST
Inp 687.00 NIST
Inp 690.00 NIST
Inp 692.00 NIST
Inp 670.10 NIST
Inp Outlier 731.30 NIST
Inp Outlier 648.00 NIST
Inp 697.00 NIST
Inp 705.00 NIST
Ip [1065.00; 1105.00]   Show Hide
Ip 1065.00 NIST
Ip 1093.00 NIST
Ip 1097.00 NIST
Ip 1100.00 NIST
Ip 1081.00 NIST
Ip 1065.00 NIST
Ip 1066.00 NIST
Ip 1085.00 NIST
Ip 1105.00 NIST
Ip 1083.00 NIST
Ip 1083.00 NIST
Ip 1068.00 NIST
Ip 1084.00 NIST
Ip 1066.00 NIST
Ip 1065.00 NIST
Ip 1065.00 NIST
Ip 1066.00 NIST
Ip 1083.00 NIST
S°gas 299.91 J/mol×K NIST
S°liquid 196.60 J/mol×K NIST
Tboil [372.00; 375.00] K Show Hide
Tboil 374.45 K Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
Tboil 374.47 K Study of isobaric vapour liquid equilibrium of some cyclic ethers with 1-chloropropane: Experimental results and SAFT-VR modelling
Tboil 374.52 K Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
Tboil 374.50 K ChemSep v8.3 pure component data Compiled value
Tboil 374.60 K KDB
Tboil 374.47 K NCMS SOLV-DB
Tboil 374.20 K NIST
Tboil 374.00 ± 0.40 K NIST
Tboil 374.50 K NIST
Tboil 374.55 ± 0.25 K NIST
Tboil 374.45 K NIST
Tboil 374.70 ± 0.30 K NIST
Tboil 374.40 ± 0.40 K NIST
Tboil 374.55 ± 0.30 K NIST
Tboil 374.25 ± 0.20 K NIST
Tboil Outlier 372.00 ± 3.00 K NIST
Tboil 374.15 ± 0.50 K NIST
Tboil 373.15 ± 1.00 K NIST
Tboil 375.00 ± 0.20 K NIST
Tboil 374.65 ± 0.50 K NIST
Tboil 374.50 ± 0.30 K NIST
Tboil 374.50 ± 0.30 K NIST
Tboil 374.15 ± 1.00 K NIST
Tboil 374.41 ± 0.10 K NIST
Tboil 374.45 ± 0.30 K NIST
Tboil 373.40 ± 0.30 K NIST
Tboil 374.60 ± 0.50 K NIST
Tboil 373.80 ± 0.50 K NIST
Tc [585.15; 588.15] K Show Hide
Tc 588.00 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 587.00 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 587.00 K ChemSep v8.3 pure component data Compiled value
Tc 587.00 K KDB
Tc 587.30 ± 1.00 K NIST
Tc 588.15 ± 2.00 K NIST
Tc 588.00 ± 2.00 K NIST
Tc Outlier 585.15 ± 2.00 K NIST
Tfus [278.54; 285.35] K Show Hide
Tfus 284.48 K Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
Tfus 284.95 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 284.95 K ChemSep v8.3 pure component data Compiled value
Tfus 284.90 K KDB
Tfus 284.95 K NCMS SOLV-DB
Tfus 284.95 ± 0.10 K NIST
Tfus 284.95 K NIST
Tfus Outlier 278.54 ± 0.10 K NIST
Tfus 284.95 ± 0.05 K NIST
Tfus 284.95 ± 0.20 K NIST
Tfus 285.35 ± 0.50 K NIST
Tfus 285.00 ± 0.20 K NIST
Tfus 284.70 ± 0.40 K NIST
Tfus 284.90 ± 0.30 K NIST
Tfus 284.91 ± 0.30 K NIST
Tfus 284.95 ± 0.20 K NIST
Tfus 284.94 ± 0.15 K NIST
Tfus 284.95 ± 0.20 K NIST
Tfus 284.15 ± 0.50 K NIST
Tfus 284.93 ± 0.02 K NIST
Tfus 283.52 ± 0.20 K NIST
Tfus 284.80 ± 0.50 K NIST
Tfus 283.20 ± 0.20 K NIST
Tfus 283.20 ± 1.50 K NIST
Ttriple [284.10; 284.95] K Show Hide
Ttriple 284.95 K ChemSep v8.3 pure component data Compiled value
Ttriple 284.10 ± 0.20 K NIST
Ttriple 284.10 ± 0.20 K NIST
UQi 2.28 ChemSep v8.3 pure component data Compiled value
URi 3.07 ChemSep v8.3 pure component data Compiled value
Vc [0.238; 0.239] m3/kmol Show Hide
Vc 0.238 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc 0.238 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.238 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.238 m3/kmol KDB
Vc 0.239 ± 0.008 m3/kmol NIST
Vc 0.239 ± 0.004 m3/kmol NIST
Zc [0.2540000; 0.2550000]   Show Hide
Zc 0.2540000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc 0.2550000 ChemSep v8.3 pure component data Compiled value
Zc 0.2540620 KDB
Zra [0.25; 0.27]   Show Hide
Zra 0.25 ChemSep v8.3 pure component data Compiled value
Zra 0.27 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [140.20; 160.40] J/mol×K [288.15; 333.15] Show Hide
Cp,liquid 146.70 J/mol×K 288.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 146.00 J/mol×K 291.00 NIST
Cp,liquid 150.00 J/mol×K 293.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 154.80 J/mol×K 296.00 NIST
Cp,liquid 147.90 J/mol×K 298.00 NIST
Cp,liquid 155.60 J/mol×K 298.00 NIST
Cp,liquid 140.20 J/mol×K 298.00 NIST
Cp,liquid 149.00 J/mol×K 298.00 NIST
Cp,liquid 149.49 J/mol×K 298.15 NIST
Cp,liquid 149.00 J/mol×K 298.15 NIST
Cp,liquid 149.65 J/mol×K 298.15 NIST
Cp,liquid 150.57 J/mol×K 298.15 NIST
Cp,liquid 151.00 J/mol×K 298.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 150.65 J/mol×K 298.15 NIST
Cp,liquid 150.77 J/mol×K 298.15 NIST
Cp,liquid 149.73 J/mol×K 298.15 NIST
Cp,liquid 147.90 J/mol×K 298.15 NIST
Cp,liquid 152.97 J/mol×K 298.20 NIST
Cp,liquid 152.10 J/mol×K 303.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 153.70 J/mol×K 308.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 155.30 J/mol×K 313.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 156.50 J/mol×K 318.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 158.40 J/mol×K 323.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 160.20 J/mol×K 328.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
Cp,liquid 160.40 J/mol×K 333.15 Thermophysical properties of dimethyl sulfoxide + cyclic and linear ethers at 308.15K Application of an extended cell model
η [0.0005770; 0.0015900] Pa×s [283.15; 353.15] Show Hide
η 0.0015900 Pa×s 283.15 Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0014400 Pa×s 288.15 Viscosity Behavior of Some Oxygen Containing Compounds
η 0.0014381 Pa×s 288.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0013120 Pa×s 293.15 Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0013111 Pa×s 293.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0012860 Pa×s 293.15 Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η 0.0012023 Pa×s 298.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0010870 Pa×s 298.15 NCMS SOLV-DB
η 0.0012236 Pa×s 298.15 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
η 0.0011780 Pa×s 298.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
η 0.0011800 Pa×s 298.15 Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η 0.0011850 Pa×s 298.15 Viscosity Behavior of Some Oxygen Containing Compounds
η 0.0011020 Pa×s 303.15 Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0010870 Pa×s 303.15 Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η 0.0010985 Pa×s 303.15 Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
η 0.0010983 Pa×s 303.15 Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
η 0.0011065 Pa×s 303.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0010219 Pa×s 308.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0010290 Pa×s 308.15 Viscosity Behavior of Some Oxygen Containing Compounds
η 0.0009985 Pa×s 308.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
η 0.0010295 Pa×s 308.15 Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
η 0.0009268 Pa×s 308.15 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
η 0.0009477 Pa×s 313.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0009575 Pa×s 313.15 Viscosities and Densities of Binary Mixtures of 1,4-Dioxane, Carbon Tetrachloride, and Butanol at 303.15 K, 308.15 K, and 313.15 K
η 0.0009460 Pa×s 313.15 Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0009340 Pa×s 313.15 Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η 0.0007991 Pa×s 318.15 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
η 0.0008909 Pa×s 318.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
η 0.0008140 Pa×s 323.15 Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η 0.0008250 Pa×s 323.15 Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0007180 Pa×s 333.15 Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η 0.0007210 Pa×s 333.15 Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0006400 Pa×s 343.15 Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
η 0.0006400 Pa×s 343.15 Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0005770 Pa×s 353.15 Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
σcond [0.00; 0.00] S/m [298.15; 323.15] Show Hide
σcond 0.00 S/m 298.15 Micellar Properties and Related Thermodynamic Parameters of the 14-6-14, 2Br- Gemini Surfactant in Water + Organic Solvent Mixed Media
σcond 0.00 S/m 303.15 Micellar Properties and Related Thermodynamic Parameters of the 14-6-14, 2Br- Gemini Surfactant in Water + Organic Solvent Mixed Media
σcond 0.00 S/m 315.15 Micellar Properties and Related Thermodynamic Parameters of the 14-6-14, 2Br- Gemini Surfactant in Water + Organic Solvent Mixed Media
σcond 0.00 S/m 323.15 Micellar Properties and Related Thermodynamic Parameters of the 14-6-14, 2Br- Gemini Surfactant in Water + Organic Solvent Mixed Media
ΔfusH [2.35; 12.84] kJ/mol [272.90; 284.10] Show Hide
ΔfusH 2.35 kJ/mol 272.90 NIST
ΔfusH 11.88 kJ/mol 283.20 NIST
ΔfusH 12.84 kJ/mol 284.10 NIST
ΔfusH 12.84 kJ/mol 284.10 NIST
ΔsubH 35.60 kJ/mol 254.50 NIST
ΔvapH [34.16; 38.00] kJ/mol [273.00; 374.50] Show Hide
ΔvapH 35.80 kJ/mol 273.00 NIST
ΔvapH 37.00 kJ/mol 318.00 NIST
ΔvapH 38.00 kJ/mol 330.00 NIST
ΔvapH 37.30 kJ/mol 345.50 NIST
ΔvapH 36.50 kJ/mol 350.50 NIST
ΔvapH 34.16 kJ/mol 374.50 NIST
ν [0.0000009; 0.0000011] m2/s [298.15; 313.15] Show Hide
ν 0.0000011 m2/s 298.15 Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
ν 0.0000009 m2/s 313.15 Experimental and predicted viscosities of binary mixtures of cyclic ethers with 1-chloropentane or 1-chlorohexane at 283.15, 298.15, and 313.15K
Pvap [2.38; 19.54] kPa [285.11; 328.15] Show Hide
Pvap 2.38 kPa 285.11 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 2.70 kPa 288.15 Vapor Pressures for 1,4-Dioxane + Tetrabutylammonium Nitrate, Water + Tetrabutylammonium Nitrate, and 1,4-Dioxane + Water + Tetrabutylammonium Nitrate
Pvap 2.92 kPa 288.66 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 3.60 kPa 292.45 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 4.50 kPa 296.56 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 4.50 kPa 296.57 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 4.90 kPa 298.15 Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
Pvap 5.08 kPa 298.15 NCMS SOLV-DB
Pvap 4.97 kPa 298.15 Vapor Pressures for 1,4-Dioxane + Tetrabutylammonium Nitrate, Water + Tetrabutylammonium Nitrate, and 1,4-Dioxane + Water + Tetrabutylammonium Nitrate
Pvap 4.90 kPa 298.15 Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
Pvap 5.34 kPa 299.81 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 6.21 kPa 302.92 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 7.58 kPa 306.93 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 7.57 kPa 306.94 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 8.12 kPa 308.15 Vapor Pressures for 1,4-Dioxane + Tetrabutylammonium Nitrate, Water + Tetrabutylammonium Nitrate, and 1,4-Dioxane + Water + Tetrabutylammonium Nitrate
Pvap 9.19 kPa 311.04 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 10.17 kPa 313.15 Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
Pvap 10.29 kPa 313.38 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 10.31 kPa 313.38 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 19.54 kPa 328.15 Isothermal (vapour + liquid) equilibrium of (cyclic ethers + chlorohexane) mixtures: Experimental results and SAFT modelling
Pvap 19.54 kPa 328.15 Isothermal vapour-liquid equilibrium for cyclic ethers with 1-chloropentane
n0 [1.40840; 1.42450]   [288.15; 318.20] Show Hide
n0 1.42450 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 1.42200 293.10 Liquid-Liquid Equilibrium for the System Water + 1,4-Dioxane + 2,6-Dimethyloct-7-en-2-ol over the Temperature Range of (343.2 to 358.2) K
n0 1.42200 293.10 Liquid liquid phase equilibria of the ternary system of water/1,4-dioxane/dihydromyrcene
n0 1.42240 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 1.41750 293.15 Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0 1.41810 298.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
n0 1.42000 298.15 NCMS SOLV-DB
n0 1.42030 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 1.42020 298.15 Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K
n0 1.41995 298.15 Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
n0 1.42020 298.15 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
n0 1.42030 298.15 Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
n0 1.42010 298.15 Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
n0 1.42030 298.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0 1.42010 298.15 Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K
n0 1.42000 298.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
n0 1.42010 298.20 Dielectric data of binary mixtures of 1,2-butanediol with 2-ethyl-1-hexanol and 1,4-dioxane at T = (298.2, 308.2, and 318.2) K
n0 1.41700 303.15 Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K
n0 1.41760 303.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
n0 1.41820 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 1.41810 303.15 Thermodynamic Properties of Water + Tetrahydrofuran and Water + 1,4-Dioxane Mixtures at (303.15, 313.15, and 323.15) K
n0 1.41700 303.15 Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
n0 1.41640 303.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0 1.41410 308.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
n0 1.41450 308.15 Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0 1.41430 308.15 Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethanediol, + Hexane, + Tributylamine, or + Triethylamine at (298.15, 303.15, and 308.15) K
n0 1.41440 308.15 Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of 1,4-Dioxane + Ethyl Acetoacetate, + Diethyl Oxalate, + Diethyl Phthalate, or + Dioctyl Phthalate at 298.15, 303.15, and 308.15 K
n0 1.41610 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 1.41430 308.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
n0 1.41440 308.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
n0 1.41420 308.20 Dielectric data of binary mixtures of 1,2-butanediol with 2-ethyl-1-hexanol and 1,4-dioxane at T = (298.2, 308.2, and 318.2) K
n0 1.41264 313.15 Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
n0 1.41390 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 1.41170 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 1.40920 318.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
n0 1.40840 318.20 Dielectric data of binary mixtures of 1,2-butanediol with 2-ethyl-1-hexanol and 1,4-dioxane at T = (298.2, 308.2, and 318.2) K
n0 1.40840 318.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
ρl [964.63; 1039.12] kg/m3 [288.15; 353.15] Show Hide
ρl 1038.78 kg/m3 288.15 Volumetric properties of binary mixtures of ethers and acetonitrile: Experimental results and application of the Prigogine Flory Patterson theory
ρl 1039.12 kg/m3 288.15 Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl 1033.00 kg/m3 293.00 KDB
ρl 1033.59 kg/m3 293.15 Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
ρl 1033.57 kg/m3 293.15 Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl 1033.50 kg/m3 293.15 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
ρl 1033.16 kg/m3 293.15 Volumetric properties of binary mixtures of ethers and acetonitrile: Experimental results and application of the Prigogine Flory Patterson theory
ρl 1033.80 kg/m3 293.15 Volumetric properties of binary mixtures of (water + organic solvents) at temperatures between T = 288.15 K and T = 303.15 K at p = 0.1 MPa
ρl 1027.92 kg/m3 298.15 Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl 1027.86 kg/m3 298.15 Study of intermolecular interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, primary amyl alcohols and 1,4-dioxane at various temperatures
ρl 1027.88 kg/m3 298.15 (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
ρl 1027.51 kg/m3 298.15 Volumetric properties of binary mixtures of ethers and acetonitrile: Experimental results and application of the Prigogine Flory Patterson theory
ρl 1027.85 kg/m3 298.15 Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
ρl 1027.94 kg/m3 298.15 Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
ρl 1027.90 kg/m3 298.15 Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
ρl 1027.85 kg/m3 298.15 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
ρl 1027.82 kg/m3 298.15 Surface Tension and Surface Properties of Binary Mixtures of 1,4-Dioxane or N,N-Dimethyl Formamide with n-Alkyl Acetates
ρl 1028.20 kg/m3 298.15 Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl 1027.99 kg/m3 298.15 Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl 1027.84 kg/m3 298.15 Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl 1027.79 kg/m3 298.15 Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl 1027.87 kg/m3 298.15 Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
ρl 1027.87 kg/m3 298.15 Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
ρl 1027.90 kg/m3 298.15 Vapour liquid equilibrium of cyclic ethers with 1-chlorohexane: Experimental results and UNIFAC predictions
ρl 1027.89 kg/m3 298.20 Temperature and concentration dependence of the relative permittivity of (1,3-butanediol + 1-octanol or 1,4-dioxane) binary liquid mixtures
ρl 1022.28 kg/m3 303.15 Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
ρl 1022.70 kg/m3 303.15 Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl 1022.30 kg/m3 303.15 Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
ρl 1022.30 kg/m3 303.15 Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
ρl 1022.40 kg/m3 303.15 Unravelling various types of non-covalent interactions of benzyl amine with ethers in n-hexane at 303.15 K by ultrasonic and DFT methods
ρl 1022.27 kg/m3 303.15 Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl 1021.84 kg/m3 303.15 Volumetric properties of binary mixtures of ethers and acetonitrile: Experimental results and application of the Prigogine Flory Patterson theory
ρl 1022.19 kg/m3 303.15 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
ρl 1022.33 kg/m3 303.15 Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl 1017.40 kg/m3 308.15 Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl 1016.57 kg/m3 308.15 Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl 1016.78 kg/m3 308.15 Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl 1016.60 kg/m3 308.15 Densities, Speeds of Sound, Excess Molar Enthalpies, and Heat Capacities of o-Chlorotoluene and Cyclic Ether Mixtures
ρl 1016.52 kg/m3 308.15 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
ρl 1016.66 kg/m3 308.15 Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl 1016.59 kg/m3 308.15 Thermodynamic Studies of Molecular Interactions in Mixtures Containing Tetrahydropyran, 1,4-dioxane and Cyclic ketones
ρl 1010.91 kg/m3 313.15 Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl 1011.10 kg/m3 313.15 Densities, Viscosities, and Sound Speed of Binary Mixtures of Hexyl Acetate with Tetrahydrofuran, 1,4-Dioxane, Anisole, and Butyl Vinyl Ether
ρl 1010.98 kg/m3 313.15 Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl 1010.83 kg/m3 313.15 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
ρl 1005.12 kg/m3 318.15 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
ρl 1005.29 kg/m3 318.15 Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl 1005.28 kg/m3 318.15 Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl 1005.24 kg/m3 318.15 Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl 999.40 kg/m3 323.15 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
ρl 999.58 kg/m3 323.15 Densities, Viscosities, and Speeds of Sound of Binary Mixtures of Heptan-1-ol with 1,4-Dioxane at Temperatures from (298.15 to 323.15) K and Atmospheric Pressure
ρl 999.49 kg/m3 323.15 Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl 987.97 kg/m3 333.15 Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl 976.37 kg/m3 343.15 Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
ρl 964.63 kg/m3 353.15 Density and Refractive Index of Binary Mixtures of Two 1-Alkyl-3-methylimidazolium Ionic Liquids with 1,4-Dioxane and Ethylene Glycol
D*i [0.00; 0.00] m2/s [288.31; 358.49] Show Hide
D*i 0.00 m2/s 288.31 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 288.33 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 293.11 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.13 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.17 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 303.12 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 307.92 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 308.06 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 317.85 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 318.24 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 327.94 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 327.95 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 338.09 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 338.12 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 338.13 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 347.87 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 347.97 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 358.25 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 358.49 Viscous Calibration Liquids for Self-diffusion Measurements
ΔfusS [8.79; 45.19] J/mol×K [272.90; 284.10] Show Hide
ΔfusS 8.79 J/mol×K 272.90 NIST
ΔfusS 41.90 J/mol×K 283.20 NIST
ΔfusS 45.19 J/mol×K 284.10 NIST
csound,fluid [1258.60; 1409.60] m/s [283.15; 318.15] Show Hide
csound,fluid 1409.60 m/s 283.15 Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
csound,fluid 1367.20 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 1357.70 m/s 295.15 Density, Speed of Sound, and Refractive Index Measurements for the Binary Mixture (1, 4-Dioxane + Isobutyric Acid) at T = (295.15, 298.15, 301.15, 304.15, 307.15, 310.15, and 313.15) K
csound,fluid 1343.60 m/s 298.15 Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
csound,fluid 1344.80 m/s 298.15 Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
csound,fluid 1344.70 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 1344.80 m/s 298.15 Density, Speed of Sound, and Refractive Index Measurements for the Binary Mixture (1, 4-Dioxane + Isobutyric Acid) at T = (295.15, 298.15, 301.15, 304.15, 307.15, 310.15, and 313.15) K
csound,fluid 1346.30 m/s 298.15 Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
csound,fluid 1331.90 m/s 301.15 Density, Speed of Sound, and Refractive Index Measurements for the Binary Mixture (1, 4-Dioxane + Isobutyric Acid) at T = (295.15, 298.15, 301.15, 304.15, 307.15, 310.15, and 313.15) K
csound,fluid 1323.10 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 1319.00 m/s 304.15 Density, Speed of Sound, and Refractive Index Measurements for the Binary Mixture (1, 4-Dioxane + Isobutyric Acid) at T = (295.15, 298.15, 301.15, 304.15, 307.15, 310.15, and 313.15) K
csound,fluid 1306.20 m/s 307.15 Density, Speed of Sound, and Refractive Index Measurements for the Binary Mixture (1, 4-Dioxane + Isobutyric Acid) at T = (295.15, 298.15, 301.15, 304.15, 307.15, 310.15, and 313.15) K
csound,fluid 1301.20 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 1293.30 m/s 310.15 Density, Speed of Sound, and Refractive Index Measurements for the Binary Mixture (1, 4-Dioxane + Isobutyric Acid) at T = (295.15, 298.15, 301.15, 304.15, 307.15, 310.15, and 313.15) K
csound,fluid 1279.70 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 1279.80 m/s 313.15 Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
csound,fluid 1278.80 m/s 313.15 Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
csound,fluid 1280.40 m/s 313.15 Density, Speed of Sound, and Refractive Index Measurements for the Binary Mixture (1, 4-Dioxane + Isobutyric Acid) at T = (295.15, 298.15, 301.15, 304.15, 307.15, 310.15, and 313.15) K
csound,fluid 1258.60 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
γ [0.03; 0.04] N/m [283.15; 313.15] Show Hide
γ 0.04 N/m 283.15 Thermophysical study of 1,4-dioxane with cycloalkane mixtures
γ 0.03 N/m 298.15 Thermophysical study of 1,4-dioxane with cycloalkane mixtures
γ 0.03 N/m 298.15 NCMS SOLV-DB
γ 0.03 N/m 313.15 Thermophysical study of 1,4-dioxane with cycloalkane mixtures

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tfus(P) 285.08 K 101.30 (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure

Datasets

  1. Viscosity, Pa*s (2)
  2. Mass density, kg/m3 (1)

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
303.15 101.33 0.0011
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
303.15 101.30 0.0010
Reference

Mass density, kg/m3

Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
85.90 298.15 1027.93
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [63.49; 281.92] J/mol×K [200.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A4.62500e+01
Coefficient B-6.13410e+02
Coefficient C5.91424e+00
Coefficient D4.78200e-06
Coefficient E-2.22380e-08
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 63.49 J/mol×K 200.00 Calculated Property
Cp,gas 108.58 J/mol×K 344.44 Calculated Property
Cp,gas 151.52 J/mol×K 488.89 Calculated Property
Cp,gas 185.99 J/mol×K 633.33 Calculated Property
Cp,gas 212.89 J/mol×K 777.78 Calculated Property
Cp,gas 233.90 J/mol×K 922.22 Calculated Property
Cp,gas 250.42 J/mol×K 1066.67 Calculated Property
Cp,gas 263.47 J/mol×K 1211.11 Calculated Property
Cp,gas 273.80 J/mol×K 1355.56 Calculated Property
Cp,gas 281.92 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [151.82; 223.75] J/mol×K [284.93; 374.47] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.51550e+02
Coefficient B-6.53140e+04
Coefficient C5.12442e+02
Coefficient D-1.34020e+00
Coefficient E1.19890e-03
Temperature range, min.284.93
Temperature range, max.374.47
Cp,liquid 151.82 J/mol×K 284.93 Calculated Property
Cp,liquid 152.55 J/mol×K 294.88 Calculated Property
Cp,liquid 154.40 J/mol×K 304.83 Calculated Property
Cp,liquid 158.09 J/mol×K 314.78 Calculated Property
Cp,liquid 164.09 J/mol×K 324.73 Calculated Property
Cp,liquid 172.45 J/mol×K 334.67 Calculated Property
Cp,liquid 182.83 J/mol×K 344.62 Calculated Property
Cp,liquid 194.80 J/mol×K 354.57 Calculated Property
Cp,liquid 208.27 J/mol×K 364.52 Calculated Property
Cp,liquid 223.75 J/mol×K 374.47 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0015088; 0.0002308] Pa×s [284.95; 487.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-7.92800e+01
Coefficient B4.19840e+03
Coefficient C1.03930e+01
Coefficient D-8.55680e-06
Coefficient E2.00000e+00
Temperature range, min.284.95
Temperature range, max.487.00
η 0.0015088 Pa×s 284.95 Calculated Property
η 0.0010097 Pa×s 307.40 Calculated Property
η 0.0007336 Pa×s 329.85 Calculated Property
η 0.0005669 Pa×s 352.30 Calculated Property
η 0.0004588 Pa×s 374.75 Calculated Property
η 0.0003844 Pa×s 397.20 Calculated Property
η 0.0003306 Pa×s 419.65 Calculated Property
η 0.0002897 Pa×s 442.10 Calculated Property
η 0.0002574 Pa×s 464.55 Calculated Property
η 0.0002308 Pa×s 487.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [39.20; 0.00] kJ/mol [274.17; 587.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A2.13670e+02
Coefficient B9.18120e+00
Coefficient C-2.29920e+01
Coefficient D2.38540e+01
Coefficient E-9.34000e+00
Critical temperature, Tc (K)5.87000e+02
CommentRange stopped at Tc; ChemSep gives it to 587.56 K.
Temperature range, min.274.17
Temperature range, max.587.00
ΔvapH 39.20 kJ/mol 274.17 Calculated Property
ΔvapH 37.57 kJ/mol 308.93 Calculated Property
ΔvapH 36.00 kJ/mol 343.69 Calculated Property
ΔvapH 34.22 kJ/mol 378.45 Calculated Property
ΔvapH 32.05 kJ/mol 413.21 Calculated Property
ΔvapH 29.44 kJ/mol 447.96 Calculated Property
ΔvapH 26.36 kJ/mol 482.72 Calculated Property
ΔvapH 22.67 kJ/mol 517.48 Calculated Property
ΔvapH 17.45 kJ/mol 552.24 Calculated Property
ΔvapH 0.00 kJ/mol 587.00 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.67] kPa [274.07; 398.83] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.48111e+01
Coefficient B-3.42606e+03
Coefficient C-3.81740e+01
Temperature range, min.274.07
Temperature range, max.398.83
Pvap 1.33 kPa 274.07 Calculated Property
Pvap 2.99 kPa 287.93 Calculated Property
Pvap 6.14 kPa 301.79 Calculated Property
Pvap 11.75 kPa 315.66 Calculated Property
Pvap 21.15 kPa 329.52 Calculated Property
Pvap 36.08 kPa 343.38 Calculated Property
Pvap 58.76 kPa 357.24 Calculated Property
Pvap 91.88 kPa 371.11 Calculated Property
Pvap 138.64 kPa 384.97 Calculated Property
Pvap 202.67 kPa 398.83 Calculated Property
Pvap [2.53; 5170.00] kPa [284.95; 580.80] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A4.32073e+01
Coefficient B-5.57721e+03
Coefficient C-4.04685e+00
Coefficient D2.08057e-06
Coefficient E2.00000e+00
CommentRange stopped where the equation exceeds Pc; ChemSep gives it to 587 K.
Temperature range, min.284.95
Temperature range, max.580.80
Pvap 2.53 kPa 284.95 Calculated Property
Pvap 12.85 kPa 317.82 Calculated Property
Pvap 46.79 kPa 350.69 Calculated Property
Pvap 133.77 kPa 383.57 Calculated Property
Pvap 319.22 kPa 416.44 Calculated Property
Pvap 663.44 kPa 449.31 Calculated Property
Pvap 1238.47 kPa 482.18 Calculated Property
Pvap 2124.21 kPa 515.05 Calculated Property
Pvap 3405.39 kPa 547.93 Calculated Property
Pvap 5170.00 kPa 580.80 Calculated Property
Pvap [1.26; 5195.37] kPa [275.00; 587.00] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A7.69176e+01
Coefficient B-7.07594e+03
Coefficient C-9.15152e+00
Coefficient D5.90158e-06
Coefficient E0.00000e+00
Temperature range, min.275.00
Temperature range, max.587.00
Pvap 1.26 kPa 275.00 Calculated Property
Pvap 8.54 kPa 309.67 Calculated Property
Pvap 36.89 kPa 344.33 Calculated Property
Pvap 116.49 kPa 379.00 Calculated Property
Pvap 294.01 kPa 413.67 Calculated Property
Pvap 630.26 kPa 448.33 Calculated Property
Pvap 1197.33 kPa 483.00 Calculated Property
Pvap 2078.30 kPa 517.67 Calculated Property
Pvap 3370.87 kPa 552.33 Calculated Property
Pvap 5195.37 kPa 587.00 Calculated Property
Pvap [3.82; 112.90] kPa [293.00; 378.00] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.51541e+01
Coefficient B-3.61527e+03
Coefficient C-3.12970e+01
ReferenceCrenshaw, Cope, et al., 1938
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.293.00
Temperature range, max.378.00
Pvap 3.82 kPa 293.00 Calculated Property
Pvap 6.18 kPa 302.44 Calculated Property
Pvap 9.68 kPa 311.89 Calculated Property
Pvap 14.72 kPa 321.33 Calculated Property
Pvap 21.81 kPa 330.78 Calculated Property
Pvap 31.54 kPa 340.22 Calculated Property
Pvap 44.64 kPa 349.67 Calculated Property
Pvap 61.91 kPa 359.11 Calculated Property
Pvap 84.31 kPa 368.56 Calculated Property
Pvap 112.90 kPa 378.00 Calculated Property
Property Value Unit Temperature (K) Source
ρl [1056.31; 341.16] kg/m3 [273.83; 587.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A8.84487e+01
Coefficient B2.59260e-01
Coefficient C5.87000e+02
Coefficient D2.82780e-01
Temperature range, min.273.83
Temperature range, max.587.00
ρl 1056.31 kg/m3 273.83 Calculated Property
ρl 1017.92 kg/m3 308.63 Calculated Property
ρl 977.51 kg/m3 343.42 Calculated Property
ρl 934.59 kg/m3 378.22 Calculated Property
ρl 888.44 kg/m3 413.02 Calculated Property
ρl 837.93 kg/m3 447.81 Calculated Property
ρl 781.12 kg/m3 482.61 Calculated Property
ρl 714.08 kg/m3 517.41 Calculated Property
ρl 626.10 kg/m3 552.20 Calculated Property
ρl 341.16 kg/m3 587.00 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.02] N/m [284.95; 374.35] Jasper (1972), surface tension of pure liquid compounds Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is γ in N/m, T in K
Coefficient A7.42252e-02
Coefficient B-1.39100e-04
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.284.95
Temperature range, max.374.35
γ 0.03 N/m 284.95 Calculated Property
γ 0.03 N/m 294.88 Calculated Property
γ 0.03 N/m 304.82 Calculated Property
γ 0.03 N/m 314.75 Calculated Property
γ 0.03 N/m 324.68 Calculated Property
γ 0.03 N/m 334.62 Calculated Property
γ 0.03 N/m 344.55 Calculated Property
γ 0.02 N/m 354.48 Calculated Property
γ 0.02 N/m 364.42 Calculated Property
γ 0.02 N/m 374.35 Calculated Property
γ [0.04; 6.17e-06] N/m [274.86; 581.38] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-1.53900e-02
Coefficient B-2.37840e+02
Coefficient C-6.81290e-01
Coefficient D-5.09840e-03
Coefficient E-3.52470e-07
CommentRange stopped where the equation turns negative; ChemSep gives it to 587 K.
Temperature range, min.274.86
Temperature range, max.581.38
γ 0.04 N/m 274.86 Calculated Property
γ 0.03 N/m 308.92 Calculated Property
γ 0.03 N/m 342.98 Calculated Property
γ 0.02 N/m 377.03 Calculated Property
γ 0.02 N/m 411.09 Calculated Property
γ 0.01 N/m 445.15 Calculated Property
γ 0.01 N/m 479.21 Calculated Property
γ 0.01 N/m 513.27 Calculated Property
γ 0.00 N/m 547.32 Calculated Property
γ 6.17e-06 N/m 581.38 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.06] W/m×K [284.95; 768.01] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A2.38730e-07
Coefficient B1.85050e+00
Coefficient C-9.45750e+01
Coefficient D7.80420e+03
Temperature range, min.284.95
Temperature range, max.768.01
λgas 0.01 W/m×K 284.95 Calculated Property
λgas 0.01 W/m×K 338.62 Calculated Property
λgas 0.02 W/m×K 392.30 Calculated Property
λgas 0.02 W/m×K 445.97 Calculated Property
λgas 0.03 W/m×K 499.64 Calculated Property
λgas 0.03 W/m×K 553.32 Calculated Property
λgas 0.04 W/m×K 606.99 Calculated Property
λgas 0.05 W/m×K 660.66 Calculated Property
λgas 0.05 W/m×K 714.34 Calculated Property
λgas 0.06 W/m×K 768.01 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.16; 0.13] W/m×K [284.95; 374.47] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A8.98340e-02
Coefficient B4.64210e+01
Coefficient C-1.18980e+00
Coefficient D-3.73380e-03
Coefficient E-6.13580e-06
Temperature range, min.284.95
Temperature range, max.374.47
λliquid 0.16 W/m×K 284.95 Calculated Property
λliquid 0.16 W/m×K 294.90 Calculated Property
λliquid 0.15 W/m×K 304.84 Calculated Property
λliquid 0.15 W/m×K 314.79 Calculated Property
λliquid 0.14 W/m×K 324.74 Calculated Property
λliquid 0.14 W/m×K 334.68 Calculated Property
λliquid 0.14 W/m×K 344.63 Calculated Property
λliquid 0.13 W/m×K 354.58 Calculated Property
λliquid 0.13 W/m×K 364.52 Calculated Property
λliquid 0.13 W/m×K 374.47 Calculated Property

Similar Compounds

1,4-Dioxyl radical. 12-Crown-4. 15-Crown-5. 1,4,7,10,13,16-Hexaoxacyclooctadecane. Ethane, 1,2-diethoxy-. Ethane, 1,1'-oxybis[2-methoxy-. 2,5,8,11,14,17,20-HEPTAOXAHENEICOSANE. 2,5,8,11-Tetraoxadodecane. 2,5,8,11,14-Pentaoxapentadecane. 2,5,8,11,14,17-Hexaoxaoctadecane. Diethyl carbitol. Triethylene glycol diethyl ether. 2,5-Dioxaheptane. Triethylene glycol diformate. Hexaethylene glycol.

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Mixtures

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Sources

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