- InChI
- InChI=1S/C6H10O4/c7-5(8)3-1-2-4-6(9)10/h1-4H2,(H,7,8)(H,9,10)
- InChI Key
- WNLRTRBMVRJNCN-UHFFFAOYSA-N
- Formula
- C6H10O4
- SMILES
- O=C(O)CCCCC(=O)O
- Molecular Weight1
- 146.14
- CAS
- 124-04-9
- Other Names
-
- 1,4-butanedicarboxylic acid
- 1,6-hexanedioic acid
- Adi-pure
- Adipinic acid
- Hexanedioc acid
- Kyselina adipova
- NSC 7622
- acifloctin
- acinetten
- adilactetten
- adipic acid
- asapic
- inipol DS
- ω : Acentric Factor.
- ΔcH°solid : Standard solid 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).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid phase 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).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation 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).
- 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.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced 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).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.0507 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | [-2802.40; -2768.70] | kJ/mol |
|
| ΔcH°solid | -2768.70 ± 5.90 | kJ/mol | NIST |
| ΔcH°solid | -2791.98 ± 0.42 | kJ/mol | NIST |
| ΔcH°solid | -2795.90 ± 0.75 | kJ/mol | NIST |
| ΔcH°solid | -2802.40 ± 1.40 | kJ/mol | NIST |
| μ | 2.32 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -682.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -865.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°solid | [-1021.32; -998.22] | kJ/mol |
|
| ΔfH°solid | -1021.32 | kJ/mol | NIST |
| ΔfH°solid | -998.22 ± 0.42 | kJ/mol | NIST |
| ΔfusH° | [33.70; 38.00] | kJ/mol |
|
| ΔfusH° | 33.70 | kJ/mol | Vaporization, fusion and sublimation enthalpies of the dicarboxylic acids from C4 to C14 and C16 |
| ΔfusH° | 38.00 | kJ/mol | Thermal analysis of phase change materials in the temperature range 120.150 .C |
| ΔsubH° | [129.00; 133.60] | kJ/mol |
|
| ΔsubH° | 133.60 ± 1.30 | kJ/mol | NIST |
| ΔsubH° | 129.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 105.20 | kJ/mol | NIST |
| IE | 10.18 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.82 | Aq. Solubility Prediction | |
| logPoct/wat | 0.716 | Crippen Calculated Property | |
| McVol | 110.280 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| Pc | [3530.00; 3850.00] | kPa |
|
| Pc | 3850.00 | kPa | Critical Temperatures and Pressures of Straight-Chain Saturated Dicarboxylic Acids (C4 to C14) |
| Pc | 3530.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 0.08 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1372.40; 1372.40] |
|
|
| Inp | 1372.40 | NIST | |
| Inp | 1372.40 | NIST | |
| Ip | 2137.00 | NIST | |
| Tboil | 611.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 809.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [422.00; 430.00] | K |
|
| Tfus | 425.50 | K | Solubilities of Adipic Acid in Cyclohexanol + Cyclohexanone Mixtures and Cyclohexanone + Cyclohexane Mixtures |
| Tfus | 424.26 | K | Determination and Thermodynamic Modeling of Solid-Liquid Phase Equilibrium for Succinic Acid in the Glutaric Acid + Adipic Acid + Ethyl Acetate Mixture and Adipic Acid in the Succinic Acid + Glutaric Acid + Ethyl Acetate Mixture |
| Tfus | 425.15 | K | Solubilities of Adipic Acid and Succinic Acid in Glutaric Acid + Acetone or n-butanol Mixture |
| Tfus | 426.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 426.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 425.95 | K | Aq. Solubility Prediction |
| Tfus | 426.07 ± 0.20 | K | NIST |
| Tfus | 425.50 ± 0.30 | K | NIST |
| Tfus | 425.50 ± 0.30 | K | NIST |
| Tfus | 425.50 ± 0.30 | K | NIST |
| Tfus | 425.50 ± 0.40 | K | NIST |
| Tfus | 425.50 ± 0.30 | K | NIST |
| Tfus | 426.00 ± 1.50 | K | NIST |
| Tfus | 425.50 ± 0.50 | K | NIST |
| Tfus | Outlier 422.00 ± 8.00 | K | NIST |
| Tfus | 422.40 ± 1.00 | K | NIST |
| Tfus | Outlier 430.00 ± 2.00 | K | NIST |
| Tfus | 424.00 ± 1.50 | K | NIST |
| Ttriple | [424.70; 425.50] | K |
|
| Ttriple | 425.50 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 424.70 ± 0.30 | K | NIST |
| Ttriple | 424.70 ± 0.30 | K | NIST |
| UQi | 4.61 | ChemSep v8.3 pure component data Compiled value | |
| URi | 5.30 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.400 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2100000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.23 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [33.70; 34.85] | kJ/mol | [419.00; 426.40] |
|
| ΔfusH | 33.70 | kJ/mol | 419.00 | NIST |
| ΔfusH | 34.85 | kJ/mol | 425.50 | NIST |
| ΔfusH | 34.85 | kJ/mol | 426.40 | NIST |
| ΔfusH | 34.85 | kJ/mol | 426.40 | NIST |
| ΔsubH | [125.00; 146.20] | kJ/mol | [296.00; 382.50] |
|
| ΔsubH | 146.20 | kJ/mol | 296.00 | NIST |
| ΔsubH | 140.00 | kJ/mol | 306.50 | NIST |
| ΔsubH | 145.00 ± 4.00 | kJ/mol | 348.00 | NIST |
| ΔsubH | 125.00 ± 20.00 | kJ/mol | 363.00 | NIST |
| ΔsubH | 129.30 ± 2.50 | kJ/mol | 382.50 | NIST |
| ΔsubH | 129.30 ± 2.50 | kJ/mol | 382.50 | NIST |
| ΔvapH | 92.00 | kJ/mol | 521.50 | NIST |
| ΔfusS | 81.92 | J/mol×K | 425.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 538.20 | K | 13.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [162.89; 381.29] | J/mol×K | [273.00; 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 | 8.54740e+01 | |||
| Coefficient B | -4.23410e+02 | |||
| Coefficient C | 5.83724e+00 | |||
| Coefficient D | 2.61780e-04 | |||
| Coefficient E | -1.14620e-07 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 162.89 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 218.53 | J/mol×K | 409.33 | Calculated Property |
| Cp,gas | 261.39 | J/mol×K | 545.67 | Calculated Property |
| Cp,gas | 294.33 | J/mol×K | 682.00 | Calculated Property |
| Cp,gas | 319.94 | J/mol×K | 818.33 | Calculated Property |
| Cp,gas | 339.94 | J/mol×K | 954.67 | Calculated Property |
| Cp,gas | 355.45 | J/mol×K | 1091.00 | Calculated Property |
| Cp,gas | 367.19 | J/mol×K | 1227.33 | Calculated Property |
| Cp,gas | 375.68 | J/mol×K | 1363.67 | Calculated Property |
| Cp,gas | 381.29 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [365.18; 402.80] | J/mol×K | [425.50; 611.00] |
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 | 2.35940e+02 | |||
| Coefficient B | -3.29970e+01 | |||
| Coefficient C | 3.90124e+00 | |||
| Coefficient D | 3.26720e-03 | |||
| Coefficient E | -1.94560e-06 | |||
| Temperature range, min. | 425.50 | |||
| Temperature range, max. | 611.00 | |||
| Cp,liquid | 365.18 | J/mol×K | 425.50 | Calculated Property |
| Cp,liquid | 369.91 | J/mol×K | 446.11 | Calculated Property |
| Cp,liquid | 374.54 | J/mol×K | 466.72 | Calculated Property |
| Cp,liquid | 379.06 | J/mol×K | 487.33 | Calculated Property |
| Cp,liquid | 383.44 | J/mol×K | 507.94 | Calculated Property |
| Cp,liquid | 387.68 | J/mol×K | 528.56 | Calculated Property |
| Cp,liquid | 391.75 | J/mol×K | 549.17 | Calculated Property |
| Cp,liquid | 395.64 | J/mol×K | 569.78 | Calculated Property |
| Cp,liquid | 399.33 | J/mol×K | 590.39 | Calculated Property |
| Cp,liquid | 402.80 | J/mol×K | 611.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0045408; 0.0026405] | Pa×s | [433.15; 466.15] |
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 | -8.47380e+00 | |||
| Coefficient B | 3.09320e+03 | |||
| Coefficient C | -6.83190e-01 | |||
| Coefficient D | 4.56680e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 433.15 | |||
| Temperature range, max. | 466.15 | |||
| η | 0.0045408 | Pa×s | 433.15 | Calculated Property |
| η | 0.0042583 | Pa×s | 436.82 | Calculated Property |
| η | 0.0039975 | Pa×s | 440.48 | Calculated Property |
| η | 0.0037566 | Pa×s | 444.15 | Calculated Property |
| η | 0.0035338 | Pa×s | 447.82 | Calculated Property |
| η | 0.0033275 | Pa×s | 451.48 | Calculated Property |
| η | 0.0031362 | Pa×s | 455.15 | Calculated Property |
| η | 0.0029587 | Pa×s | 458.82 | Calculated Property |
| η | 0.0027938 | Pa×s | 462.48 | Calculated Property |
| η | 0.0026405 | Pa×s | 466.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [93.05; 0.00] | kJ/mol | [425.50; 809.00] |
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 | 1.94925e+02 | |||
| Coefficient B | 8.23008e-01 | |||
| Coefficient C | 2.51816e+00 | |||
| Coefficient D | -5.64633e+00 | |||
| Coefficient E | 2.78457e+00 | |||
| Critical temperature, Tc (K) | 8.09000e+02 | |||
| Temperature range, min. | 425.50 | |||
| Temperature range, max. | 809.00 | |||
| ΔvapH | 93.05 | kJ/mol | 425.50 | Calculated Property |
| ΔvapH | 87.33 | kJ/mol | 468.11 | Calculated Property |
| ΔvapH | 82.39 | kJ/mol | 510.72 | Calculated Property |
| ΔvapH | 78.02 | kJ/mol | 553.33 | Calculated Property |
| ΔvapH | 73.88 | kJ/mol | 595.94 | Calculated Property |
| ΔvapH | 69.50 | kJ/mol | 638.56 | Calculated Property |
| ΔvapH | 64.13 | kJ/mol | 681.17 | Calculated Property |
| ΔvapH | 56.47 | kJ/mol | 723.78 | Calculated Property |
| ΔvapH | 43.61 | kJ/mol | 766.39 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 809.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [479.40; 639.57] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.76921e+01 | |||
| Coefficient B | -6.86994e+03 | |||
| Coefficient C | -8.46730e+01 | |||
| Temperature range, min. | 479.40 | |||
| Temperature range, max. | 639.57 | |||
| Pvap | 1.33 | kPa | 479.40 | Calculated Property |
| Pvap | 2.83 | kPa | 497.20 | Calculated Property |
| Pvap | 5.63 | kPa | 514.99 | Calculated Property |
| Pvap | 10.61 | kPa | 532.79 | Calculated Property |
| Pvap | 19.05 | kPa | 550.59 | Calculated Property |
| Pvap | 32.77 | kPa | 568.38 | Calculated Property |
| Pvap | 54.24 | kPa | 586.18 | Calculated Property |
| Pvap | 86.74 | kPa | 603.98 | Calculated Property |
| Pvap | 134.46 | kPa | 621.77 | Calculated Property |
| Pvap | 202.66 | kPa | 639.57 | Calculated Property |
| Pvap | [0.08; 3530.00] | kPa | [425.50; 785.68] |
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 | 2.48316e+02 | |||
| Coefficient B | -2.32339e+04 | |||
| Coefficient C | -3.28308e+01 | |||
| Coefficient D | 1.34350e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 809 K. | |||
| Temperature range, min. | 425.50 | |||
| Temperature range, max. | 785.68 | |||
| Pvap | 0.08 | kPa | 425.50 | Calculated Property |
| Pvap | 0.69 | kPa | 465.52 | Calculated Property |
| Pvap | 4.05 | kPa | 505.54 | Calculated Property |
| Pvap | 17.01 | kPa | 545.56 | Calculated Property |
| Pvap | 56.16 | kPa | 585.58 | Calculated Property |
| Pvap | 155.57 | kPa | 625.60 | Calculated Property |
| Pvap | 379.37 | kPa | 665.62 | Calculated Property |
| Pvap | 844.36 | kPa | 705.64 | Calculated Property |
| Pvap | 1763.33 | kPa | 745.66 | Calculated Property |
| Pvap | 3530.00 | kPa | 785.68 | Calculated Property |
| Pvap | [0.08; 102.59] | kPa | [425.50; 611.15] |
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 | 1.33029e+02 | |||
| Coefficient B | -1.71566e+04 | |||
| Coefficient C | -1.58264e+01 | |||
| Coefficient D | 3.22958e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 425.50 | |||
| Temperature range, max. | 611.15 | |||
| Pvap | 0.08 | kPa | 425.50 | Calculated Property |
| Pvap | 0.26 | kPa | 446.13 | Calculated Property |
| Pvap | 0.75 | kPa | 466.76 | Calculated Property |
| Pvap | 1.90 | kPa | 487.38 | Calculated Property |
| Pvap | 4.41 | kPa | 508.01 | Calculated Property |
| Pvap | 9.40 | kPa | 528.64 | Calculated Property |
| Pvap | 18.65 | kPa | 549.27 | Calculated Property |
| Pvap | 34.72 | kPa | 569.89 | Calculated Property |
| Pvap | 61.16 | kPa | 590.52 | Calculated Property |
| Pvap | 102.59 | kPa | 611.15 | Calculated Property |
| Pvap | [0.13; 101.89] | kPa | [432.70; 610.70] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.72074e+01 | |||
| Coefficient B | -6.47732e+03 | |||
| Coefficient C | -9.59510e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 432.70 | |||
| Temperature range, max. | 610.70 | |||
| Pvap | 0.13 | kPa | 432.70 | Calculated Property |
| Pvap | 0.38 | kPa | 452.48 | Calculated Property |
| Pvap | 0.99 | kPa | 472.26 | Calculated Property |
| Pvap | 2.35 | kPa | 492.03 | Calculated Property |
| Pvap | 5.11 | kPa | 511.81 | Calculated Property |
| Pvap | 10.37 | kPa | 531.59 | Calculated Property |
| Pvap | 19.78 | kPa | 551.37 | Calculated Property |
| Pvap | 35.75 | kPa | 571.14 | Calculated Property |
| Pvap | 61.63 | kPa | 590.92 | Calculated Property |
| Pvap | 101.89 | kPa | 610.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1090.99; 365.36] | kg/m3 | [425.50; 809.00] |
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 | 9.46951e+01 | |||
| Coefficient B | 2.59180e-01 | |||
| Coefficient C | 8.09000e+02 | |||
| Coefficient D | 2.81980e-01 | |||
| Temperature range, min. | 425.50 | |||
| Temperature range, max. | 809.00 | |||
| ρl | 1090.99 | kg/m3 | 425.50 | Calculated Property |
| ρl | 1052.69 | kg/m3 | 468.11 | Calculated Property |
| ρl | 1012.32 | kg/m3 | 510.72 | Calculated Property |
| ρl | 969.37 | kg/m3 | 553.33 | Calculated Property |
| ρl | 923.11 | kg/m3 | 595.94 | Calculated Property |
| ρl | 872.39 | kg/m3 | 638.56 | Calculated Property |
| ρl | 815.19 | kg/m3 | 681.17 | Calculated Property |
| ρl | 747.48 | kg/m3 | 723.78 | Calculated Property |
| ρl | 658.28 | kg/m3 | 766.39 | Calculated Property |
| ρl | 365.36 | kg/m3 | 809.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.02; 6.44e-06] | N/m | [425.50; 806.70] |
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 | -1.82660e-02 | |||
| Coefficient B | 1.23310e+02 | |||
| Coefficient C | -3.41480e+00 | |||
| Coefficient D | 5.01630e-04 | |||
| Coefficient E | -1.75960e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 809 K. | |||
| Temperature range, min. | 425.50 | |||
| Temperature range, max. | 806.70 | |||
| γ | 0.02 | N/m | 425.50 | Calculated Property |
| γ | 0.02 | N/m | 467.86 | Calculated Property |
| γ | 0.02 | N/m | 510.21 | Calculated Property |
| γ | 0.01 | N/m | 552.57 | Calculated Property |
| γ | 0.01 | N/m | 594.92 | Calculated Property |
| γ | 0.01 | N/m | 637.28 | Calculated Property |
| γ | 0.01 | N/m | 679.63 | Calculated Property |
| γ | 0.00 | N/m | 721.99 | Calculated Property |
| γ | 0.00 | N/m | 764.34 | Calculated Property |
| γ | 6.44e-06 | N/m | 806.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.05] | W/m×K | [274.00; 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 | 1.98460e-04 | |||
| Coefficient B | 8.77120e-01 | |||
| Coefficient C | 5.20450e+02 | |||
| Coefficient D | 6.20130e+04 | |||
| Temperature range, min. | 274.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 274.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 354.67 | Calculated Property |
| λgas | 0.02 | W/m×K | 435.33 | Calculated Property |
| λgas | 0.02 | W/m×K | 516.00 | Calculated Property |
| λgas | 0.03 | W/m×K | 596.67 | Calculated Property |
| λgas | 0.03 | W/m×K | 677.33 | Calculated Property |
| λgas | 0.04 | W/m×K | 758.00 | Calculated Property |
| λgas | 0.04 | W/m×K | 838.67 | Calculated Property |
| λgas | 0.05 | W/m×K | 919.33 | Calculated Property |
| λgas | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.20; 0.11] | W/m×K | [242.70; 642.70] |
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 | -1.51380e-01 | |||
| Coefficient B | 3.17230e+01 | |||
| Coefficient C | -1.14170e+00 | |||
| Coefficient D | 7.24020e-05 | |||
| Coefficient E | -7.24670e-07 | |||
| Temperature range, min. | 242.70 | |||
| Temperature range, max. | 642.70 | |||
| λliquid | 0.20 | W/m×K | 242.70 | Calculated Property |
| λliquid | 0.19 | W/m×K | 287.14 | Calculated Property |
| λliquid | 0.18 | W/m×K | 331.59 | Calculated Property |
| λliquid | 0.17 | W/m×K | 376.03 | Calculated Property |
| λliquid | 0.16 | W/m×K | 420.48 | Calculated Property |
| λliquid | 0.15 | W/m×K | 464.92 | Calculated Property |
| λliquid | 0.14 | W/m×K | 509.37 | Calculated Property |
| λliquid | 0.13 | W/m×K | 553.81 | Calculated Property |
| λliquid | 0.12 | W/m×K | 598.26 | Calculated Property |
| λliquid | 0.11 | W/m×K | 642.70 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexanedioic acid.
Mixtures
- Hexanedioic acid + Ethanol
- Hexanedioic acid + Acetic acid
- Hexanedioic acid + Acetone
- Hexanedioic acid + Ethyl Acetate
- Hexanedioic acid + Water
- Hexanedioic acid + Acetic acid + Water
- Cyclohexanol + Hexanedioic acid
- Hexanedioic acid + Cyclohexanone
- Cyclohexanol + Hexanedioic acid + Cyclohexane
- Hexanedioic acid + Cyclohexanone + Cyclohexane
- Cyclohexanol + Hexanedioic acid + Cyclohexanone
- Hexanedioic acid + Ethanol + Pentanedioic acid
- Hexanedioic acid + Propanoic acid + Water
- Hexanedioic acid + Propanoic acid
- Hexanedioic acid + Ethanol, 2,2'-oxybis-
- Hexanedioic acid + Urea + Ethanol, 2,2'-oxybis-
- Hexanedioic acid + Ethyl Acetate + Pentanedioic acid
- Hexanedioic acid + Acetic acid + Cyclohexanone
- Hexanedioic acid + Urea + Water
- Hexanedioic acid + 2-Oxepanone + Acetic acid
Find more mixtures with Hexanedioic acid.
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).
- Cheméo Relay (1.0)
- 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.
- Crippen Method
- Measurement on the solubility of adipic acid in various solvents at high temperature and its thermodynamics parameters.
- Determination and correlation of solid-liquid phase equilibrium and phase diagram for multicomponent system of mixed dibasic acids. (I) Ternary system of adipic acid + glutaric acid + ethanol system
- Determination and modeling of binary and ternary solid-liquid phase equilibrium for the systems formed by adipic acid, urea and diethylene glycol
- Solubilities of adipic acid in binary cyclohexanone + cyclohexanol, cyclohexane + cyclohexanol, and cyclohexane + cyclohexanone solvent mixtures
- Vaporization, fusion and sublimation enthalpies of the dicarboxylic acids from C4 to C14 and C16
- An odd-even effect on solubility of dicarboxylic acids in organic solvents
- Solubility and thermodynamics of vitamin C in binary liquid mixtures involving water, methanol, ethanol and isopropanol at different temperatures
- Solubility of succinic acid, glutaric acid and adipic acid in propionic acid + epsilon-caprolactone + water mixtures: Experimental measurement and thermodynamic modeling
- Thermal analysis of phase change materials in the temperature range 120.150 .C
- Solubilities of Adipic Acid in Cyclohexanol + Cyclohexanone Mixtures and Cyclohexanone + Cyclohexane Mixtures
- Determination and Correlation of Solid Liquid Phase Equilibrium and Phase Diagram for a Multicomponent System of Mixed Dibasic Acids. Ternary System of Succinic Acid + Adipic Acid + Ethanol
- Determination and Correlation of Solubilities for Succinic Acid in the Adipic Acid + Glutaric Acid + Acetone Mixture and Adipic Acid in the Succinic Acid + Glutaric Acid + Acetone Mixture
- Measurement and Correlation for Solubilities of Adipic Acid in Acetic Acid + e-Caprolactone Mixtures and Cyclohexanone + e-Caprolactone Mixtures
- Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid and Succinic Acid in Acetic Acid + Cyclohexanone Mixtures
- Measurement and Correlation for Solubilities of Adipic Acid, Glutaric Acid, and Succinic Acid in Dimethyl Adipate + Methanol Mixtures
- Measurement and Correlation for the Solubility of Adipic Acid and Succinic Acid in Glutaric Acid + Cyclohexanone and Glutaric Acid + Acetic Acid Mixtures
- Determination and Thermodynamic Modeling of Solid-Liquid Phase Equilibrium for Succinic Acid in the Glutaric Acid + Adipic Acid + Ethyl Acetate Mixture and Adipic Acid in the Succinic Acid + Glutaric Acid + Ethyl Acetate Mixture
- Phase Equilibrium Involving Xylose, Water, and Ethylene Glycol or 1,2-Propylene Glycol at Different Temperatures
- Critical Temperatures and Pressures of Straight-Chain Saturated Dicarboxylic Acids (C4 to C14)
- Viscosity B Coefficients and Activation Parameters of Viscous Flow for Hexanedioic Acid in Aqueous Dextran Solution
- Solubilities of Adipic Acid in Acetic Acid + Water Mixtures and Acetic Acid + Cyclohexane Mixtures
- Solid Liquid Equilibrium and Phase Diagram for the Ternary Succinic Acid + Glutaric Acid + Water System
- Solubilities of Adipic Acid and Succinic Acid in Glutaric Acid + Acetone or n-butanol Mixture
- Ternary Phase Diagram for Systems of Succinic Acid + Urea + Water, Glutaric Acid + Urea + Water and Adipic Acid + Urea + Water at 288.15 K and 303.15 K
- Solubility of Adipic Acid in Acetone, Chloroform, and Toluene
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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