- InChI
- InChI=1S/C6H6O2/c7-5-2-1-3-6(8)4-5/h1-4,7-8H
- InChI Key
- GHMLBKRAJCXXBS-UHFFFAOYSA-N
- Formula
- C6H6O2
- SMILES
- Oc1cccc(O)c1
- Molecular Weight1
- 110.11
- CAS
- 108-46-3
- Other Names
-
- 1,3-Benzenediol
- 1,3-Dihydroxybenzene
- 1,3-Dihydroxybenzene (resorcinol)
- 3-HYDROXYPHENOL
- Benzene, 1,3-dihydroxy-
- Benzene, m-dihydroxy-
- C.I. 76505
- C.I. Developer 4
- C.I. Oxidation Base 31
- Developer O
- Developer R
- Developer RS
- Durafur Developer G
- Fouramine RS
- Fourrine 79
- Fourrine EW
- M-DIHYDROXYBENZENE
- NCI-C05970
- NSC 1571
- Nako TGG
- Pelagol Grey RS
- Pelagol RS
- Phenol, m-hydroxy-
- Rcra waste number U201
- Resorcin
- Resorcine
- Rodol RS
- UN 2876
- m-Benzenediol
- m-Dioxybenzene
- m-Hydroquinone
- m-Hydroxyphenol
- «alpha»-Resorcinol
- «alpha»-Resorcinol
- PAff : Proton affinity (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- SProt : Protonation entropy at 298K (J/mol×K).
- 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).
- Psub : Sublimation pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 856.40 | kJ/mol | NIST |
| ΔcH°solid | [-2867.00; -2847.90] | kJ/mol |
|
| ΔcH°solid | -2847.90 ± 1.10 | kJ/mol | NIST |
| ΔcH°solid | -2850.60 ± 0.42 | kJ/mol | NIST |
| ΔcH°solid | -2867.00 | kJ/mol | NIST |
| ΔcH°solid | -2861.00 | kJ/mol | NIST |
| SProt | -15.00 | J/mol×K | NIST |
| ΔfG° | -187.56 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-284.70; -265.20] | kJ/mol |
|
| ΔfH°gas | -284.70 ± 1.20 | kJ/mol | NIST |
| ΔfH°gas | -275.00 | kJ/mol | NIST |
| ΔfH°gas | -265.20 | kJ/mol | NIST |
| ΔfH°solid | [-370.70; -351.20] | kJ/mol |
|
| ΔfH°solid | -370.70 ± 1.10 | kJ/mol | NIST |
| ΔfH°solid | -368.00 ± 0.50 | kJ/mol | NIST |
| ΔfH°solid | -351.20 | kJ/mol | NIST |
| ΔfusH° | 17.29 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [86.00; 93.00] | kJ/mol |
|
| ΔsubH° | 86.00 ± 0.52 | kJ/mol | NIST |
| ΔsubH° | 86.00 | kJ/mol | NIST |
| ΔsubH° | 87.50 ± 0.50 | kJ/mol | NIST |
| ΔsubH° | 93.00 | kJ/mol | NIST |
| ΔvapH° | 78.40 ± 1.30 | kJ/mol | NIST |
| IE | [8.20; 8.63] | eV |
|
| IE | 8.20 | eV | NIST |
| IE | 8.63 | eV | NIST |
| log10WS | [0.81; 0.81] |
|
|
| log10WS | 0.81 | Aq. Sol... | |
| log10WS | 0.81 | Estimat... | |
| logPoct/wat | 1.098 | Crippen Calculated Property | |
| McVol | 83.380 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| Pc | 6240.00 | kPa | Critica... |
| Inp | [213.50; 1379.00] |
|
|
| Inp | 1379.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 1368.00 | NIST | |
| Inp | 213.50 | NIST | |
| Inp | 216.79 | NIST | |
| Inp | 219.64 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 213.50 | NIST | |
| Inp | 1368.00 | NIST | |
| Tboil | [549.05; 554.55] | K |
|
| Tboil | 549.05 | K | KDB |
| Tboil | 550.00 | K | NIST |
| Tboil | 549.10 ± 0.40 | K | NIST |
| Tboil | 554.55 ± 0.50 | K | NIST |
| Tc | 766.85 | K | Joback Calculated Property |
| Tfus | [382.00; 383.90] | K |
|
| Tfus | 382.85 | K | KDB |
| Tfus | 383.90 | K | Aq. Sol... |
| Tfus | 383.15 | K | Liquid ... |
| Tfus | 382.00 | K | Enthalp... |
| Tfus | 383.65 | K | Thermal... |
| Ttriple | [382.70; 383.54] | K |
|
| Ttriple | 383.54 ± 0.02 | K | NIST |
| Ttriple | 382.70 ± 0.20 | K | NIST |
| Ttriple | 382.80 ± 0.25 | K | NIST |
| Vc | 0.196 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [186.33; 226.33] | J/mol×K | [519.62; 766.85] |
|
| Cp,gas | 186.33 | J/mol×K | 519.62 | Joback Calculated Property |
| Cp,gas | 194.85 | J/mol×K | 560.83 | Joback Calculated Property |
| Cp,gas | 202.41 | J/mol×K | 602.03 | Joback Calculated Property |
| Cp,gas | 209.18 | J/mol×K | 643.24 | Joback Calculated Property |
| Cp,gas | 215.32 | J/mol×K | 684.44 | Joback Calculated Property |
| Cp,gas | 220.99 | J/mol×K | 725.65 | Joback Calculated Property |
| Cp,gas | 226.33 | J/mol×K | 766.85 | Joback Calculated Property |
| Cp,solid | [131.00; 151.00] | J/mol×K | [297.90; 323.00] |
|
| Cp,solid | 131.40 | J/mol×K | 297.90 | NIST |
| Cp,solid | 131.00 | J/mol×K | 298.00 | NIST |
| Cp,solid | 135.53 | J/mol×K | 298.15 | NIST |
| Cp,solid | 139.30 | J/mol×K | 298.15 | NIST |
| Cp,solid | 151.00 | J/mol×K | 323.00 | NIST |
| η | [0.0000251; 0.0009603] | Pa×s | [394.72; 519.62] |
|
| η | 0.0009603 | Pa×s | 394.72 | Joback Calculated Property |
| η | 0.0004493 | Pa×s | 415.54 | Joback Calculated Property |
| η | 0.0002260 | Pa×s | 436.35 | Joback Calculated Property |
| η | 0.0001210 | Pa×s | 457.17 | Joback Calculated Property |
| η | 0.0000684 | Pa×s | 477.99 | Joback Calculated Property |
| η | 0.0000406 | Pa×s | 498.80 | Joback Calculated Property |
| η | 0.0000251 | Pa×s | 519.62 | Joback Calculated Property |
| ΔfusH | [1.20; 21.30] | kJ/mol | [366.80; 382.90] |
|
| ΔfusH | 1.20 | kJ/mol | 366.80 | NIST |
| ΔfusH | 20.50 | kJ/mol | 381.00 | NIST |
| ΔfusH | 18.90 | kJ/mol | 382.60 | NIST |
| ΔfusH | 18.90 | kJ/mol | 382.60 | NIST |
| ΔfusH | 21.30 | kJ/mol | 382.80 | NIST |
| ΔfusH | 21.30 | kJ/mol | 382.90 | NIST |
| ΔsubH | [85.30; 95.00] | kJ/mol | [303.00; 353.50] |
|
| ΔsubH | 93.40 | kJ/mol | 303.00 | NIST |
| ΔsubH | 95.00 ± 1.00 | kJ/mol | 329.00 | NIST |
| ΔsubH | 93.00 ± 21.00 | kJ/mol | 329.50 | NIST |
| ΔsubH | 85.30 ± 0.50 | kJ/mol | 334.00 | NIST |
| ΔsubH | 92.30 | kJ/mol | 353.50 | NIST |
| ΔvapH | [74.30; 74.30] | kJ/mol | [427.50; 484.50] |
|
| ΔvapH | 74.30 | kJ/mol | 427.50 | NIST |
| ΔvapH | 74.30 | kJ/mol | 484.50 | NIST |
| Psub | [4.00e-04; 0.02] | kPa | [323.10; 364.30] |
|
| Psub | 4.00e-04 | kPa | 323.10 | Di-Hydr... |
| Psub | 5.48e-04 | kPa | 326.10 | Di-Hydr... |
| Psub | 6.17e-04 | kPa | 326.70 | Di-Hydr... |
| Psub | 7.74e-04 | kPa | 329.10 | Di-Hydr... |
| Psub | 8.81e-04 | kPa | 330.10 | Di-Hydr... |
| Psub | 9.66e-04 | kPa | 331.20 | Di-Hydr... |
| Psub | 1.06e-03 | kPa | 332.10 | Di-Hydr... |
| Psub | 1.24e-03 | kPa | 333.30 | Di-Hydr... |
| Psub | 1.34e-03 | kPa | 334.20 | Di-Hydr... |
| Psub | 1.47e-03 | kPa | 335.20 | Di-Hydr... |
| Psub | 1.86e-03 | kPa | 337.10 | Di-Hydr... |
| Psub | 2.23e-03 | kPa | 339.30 | Di-Hydr... |
| Psub | 2.54e-03 | kPa | 340.30 | Di-Hydr... |
| Psub | 2.72e-03 | kPa | 341.20 | Di-Hydr... |
| Psub | 2.71e-03 | kPa | 341.30 | Di-Hydr... |
| Psub | 3.40e-03 | kPa | 343.30 | Di-Hydr... |
| Psub | 3.41e-03 | kPa | 343.50 | Di-Hydr... |
| Psub | 3.54e-03 | kPa | 344.30 | Di-Hydr... |
| Psub | 3.67e-03 | kPa | 344.40 | Di-Hydr... |
| Psub | 4.58e-03 | kPa | 346.20 | Di-Hydr... |
| Psub | 4.68e-03 | kPa | 346.40 | Di-Hydr... |
| Psub | 5.53e-03 | kPa | 348.30 | Di-Hydr... |
| Psub | 5.56e-03 | kPa | 348.40 | Di-Hydr... |
| Psub | 5.69e-03 | kPa | 349.30 | Di-Hydr... |
| Psub | 6.49e-03 | kPa | 350.20 | Di-Hydr... |
| Psub | 6.43e-03 | kPa | 350.30 | Di-Hydr... |
| Psub | 7.32e-03 | kPa | 351.30 | Di-Hydr... |
| Psub | 7.73e-03 | kPa | 352.20 | Di-Hydr... |
| Psub | 8.71e-03 | kPa | 353.30 | Di-Hydr... |
| Psub | 9.84e-03 | kPa | 354.30 | Di-Hydr... |
| Psub | 0.01 | kPa | 355.20 | Di-Hydr... |
| Psub | 0.01 | kPa | 356.30 | Di-Hydr... |
| Psub | 0.01 | kPa | 357.40 | Di-Hydr... |
| Psub | 0.01 | kPa | 358.20 | Di-Hydr... |
| Psub | 0.01 | kPa | 358.60 | Di-Hydr... |
| Psub | 0.02 | kPa | 360.20 | Di-Hydr... |
| Psub | 0.02 | kPa | 360.40 | Di-Hydr... |
| Psub | 0.02 | kPa | 361.30 | Di-Hydr... |
| Psub | 0.02 | kPa | 364.30 | Di-Hydr... |
| ΔfusS | [3.27; 55.60] | J/mol×K | [366.80; 382.80] |
|
| ΔfusS | 3.27 | J/mol×K | 366.80 | NIST |
| ΔfusS | 53.80 | J/mol×K | 381.00 | NIST |
| ΔfusS | 49.41 | J/mol×K | 382.60 | NIST |
| ΔfusS | 55.60 | J/mol×K | 382.80 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [444.70; 456.80] | K | [2.95; 4.93] |
|
| Tboil | 444.70 | K | 2.95 | Vapour ... |
| Tboil | 451.30 | K | 3.93 | Vapour ... |
| Tboil | 456.80 | K | 4.93 | Vapour ... |
| Tboilr | 451.20 | K | 2.10 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.09; 7618.13] | kPa | [382.00; 810.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.64521e+02 | |||
| Coefficient B | -1.68432e+04 | |||
| Coefficient C | -2.08308e+01 | |||
| Coefficient D | 7.18739e-06 | |||
| Temperature range, min. | 382.00 | |||
| Temperature range, max. | 810.00 | |||
| Pvap | 0.09 | kPa | 382.00 | Calculated Property |
| Pvap | 1.41 | kPa | 429.56 | Calculated Property |
| Pvap | 10.76 | kPa | 477.11 | Calculated Property |
| Pvap | 51.35 | kPa | 524.67 | Calculated Property |
| Pvap | 176.66 | kPa | 572.22 | Calculated Property |
| Pvap | 481.64 | kPa | 619.78 | Calculated Property |
| Pvap | 1111.85 | kPa | 667.33 | Calculated Property |
| Pvap | 2278.49 | kPa | 714.89 | Calculated Property |
| Pvap | 4290.69 | kPa | 762.44 | Calculated Property |
| Pvap | 7618.13 | kPa | 810.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Resorcinol.
Mixtures
- Resorcinol + Choline chloride
- Resorcinol + Benzene, 1,4-diiodo-
- Resorcinol + Water
- Resorcinol + Ethanol
- 1-Propanol + Resorcinol
- Resorcinol + 1-Butanol
- Resorcinol + Water + Niacinamide
- Resorcinol + Carbon dioxide
- Resorcinol + Carbon dioxide + 1,2-Benzenediol
- Resorcinol + 2-Butanone, 3-methyl- + Water
- Methyl Isobutyl Ketone + Resorcinol + Water
- Resorcinol + 2-Pentanone + Water
- Resorcinol + 2-Octanone + Water
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Partial Molar Volumes and Viscosity B-Coefficients of Nicotinamide in Aqueous Resorcinol Solutions at T=(298.15, 308.15, and 318.15)K
- Ternary liquid-liquid equilibria for methyl isopropyl ketone + (resorcinol or hydroquinone) + water systems at different temperatures
- Liquid-liquid equilibrium for ternary systems, methyl isobutyl ketone +(catechol, resorcinol and hydroquinone) + water at 333.15 K, 343.15 K and 353.15 K
- Liquid pharmaceuticals formulation by eutectic formation
- Effects of structural isomerism on solution behaviour of solutes: Apparent molar volumes and isentropic compression of catechol, resorcinal, and hydroquinone in aqueous solution at T = (283.15, 293.15, 298.15, 303.15, and 313.15) K
- Enthalpies of formation of dihydroxybenzenes revisited: Combining experimental and high-level ab initio data
- Experimental result and data correlation of liquid-liquid equilibrium for methyl isopropyl ketone + o, m, p-dihydroxybenzene + water at 333.15 K, 343.15 K and 353.15 K
- Vapour pressure data for 2-n-propylresorcinol, 4-ethylresorcinol and 4-hexylresorcinol near their normal boiling points measured by differential scanning calorimetry
- Di-Hydroxybenzenes: Catechol, Resorcinol, and Hydroquinone. Enthalpies of Phase Transitions Revisited
- Thermal, physicochemical and microstructural studies of organic analog of nonmetal-nonmetal monotectic alloy
- Solubilities of resorcinol and pyrocathecol and their mixture in supercritical carbon dioxide
- Liquid-Liquid Equilibria for Ternary (Methyl Propyl Ketone + Hydroquinone or Resorcinol + Water) Systems at 298.15, 318.15, and 333.15 K
- Liquid Liquid Equilibria for Octan-2-one + Dihydroxybenzene + Water at Different Temperatures: Experimental Data and Thermodynamic Modeling
- Measurements and Thermodynamic Modeling of Liquid-Liquid Equilibria Data for the Ternary (Methyl Propyl Ketone + Catechol/Resorcinol/Hydroquinone + Water) Systems
- Critical Point and Vapor Pressure Measurements for Four Compounds by a Low Residence Time Flow Method
- Densities and Viscosities of Binary Solutions of Benzene-1,3-diol + Water, Ethanol, Propan-1-ol, and Butan-1-ol at T = (293.15 to 333.15) K
- Liquid Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + m-Benzenediol + Water
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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