- InChI
- InChI=1S/C15H16O2/c1-15(2,11-3-7-13(16)8-4-11)12-5-9-14(17)10-6-12/h3-10,16-17H,1-2H3
- InChI Key
- IISBACLAFKSPIT-UHFFFAOYSA-N
- Formula
- C15H16O2
- SMILES
- CC(C)(c1ccc(O)cc1)c1ccc(O)cc1
- Molecular Weight1
- 228.29
- CAS
- 80-05-7
- Other Names
-
- 2,2-(4',4''-dihydroxy)diphenylpropane
- 2,2-(4,4'-Dihydroxydiphenyl)propane
- 2,2-(4,4-Dihydroxydiphenyl)propane
- 2,2-Bis (4-hydroxyphenol) propane
- 2,2-Bis(4'-hydroxyphenyl)propane
- 2,2-Bis(4,4'-hydroxyphenyl)propane
- 2,2-Bis(hydroxyphenyl)propane
- 2,2-Bis(p-hydroxyphenyl)propane
- 2,2-Bis-4'-hydroxyfenylpropan
- 2,2-Di(4-hydroxyphenyl)propane
- 2,2-Di(4-phenylol)propane
- 2,2-bis(4-hydroxyphenyl)propane
- 2,2-di-(4'-Hydroxyphenyl)-propane
- 2,2-di-(4-hydroxyphenyl)propane
- 4,4'-(1-METHYLETHYLIDENE)BIS-PHENOL
- 4,4'-(1-methylethylidene)bisphenol
- 4,4'-(propane-2,2-diyl)diphenol
- 4,4'-Bisphenol A
- 4,4'-Dihydroxdiphenylpropane
- 4,4'-Dihydroxy-2,2-diphenylpropane
- 4,4'-Dihydroxydiphenyl-2,2-propane
- 4,4'-Dihydroxydiphenyldimethylmethane
- 4,4'-Dihydroxydiphenylpropane
- 4,4'-ISOPROPYLIDENEDI-PHENOL
- 4,4'-Isopropylidenebis[phenol]
- 4,4'-Isopropylidenediphenol
- 4,4-isopropylidenediphenol
- BPA 157
- Biphenol A
- Bis(4-hydroxyphenyl) dimethylmethane
- Bis(p-hydroxyphenyl)propane
- Bisferol A
- Bisphenol
- Bisphenol A
- Dian
- Diano
- Dimethyl bis(p-hydroxyphenyl)methane
- Dimethylmethylene-p,p'-diphenol
- Diphenylolpropane
- Ipognox 88
- Isopropylidenebis(4-hydroxybenzene)
- NCI-C50635
- Parabis
- Parabis A
- Phenol, (1-methylethylidene)bis-
- Phenol, 4,4'-dimethylmethylenedi-
- Phenol, 4,4'-isopropylidenedi-
- Pluracol 245
- Propane, 2,2-bis(p-hydroxyphenyl)-
- Rikabanol
- di-2,2-(4-Hydroxyphenyl)propane
- p,p'-Bisphenol A
- p,p'-Dihydroxydiphenyldimethylmethane
- p,p'-Isopropylidenebisphenol
- p,p'-Isopropylidenediphenol
- p,p'-dihydroxydiphenylpropane
- «beta»,«beta»'-Bis(p-hydroxyphenyl)propane
- «beta»-di-p-hydroxyphenylpropane
- 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).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- 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).
- 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).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- 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.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.9455 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | [-7840.00; -7820.70] | kJ/mol |
|
| ΔcH°solid | -7840.00 ± 1.70 | kJ/mol | NIST |
| ΔcH°solid | -7820.70 ± 1.70 | kJ/mol | NIST |
| ΔfG° | 44.20 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -246.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°solid | [-368.60; -349.40] | kJ/mol |
|
| ΔfH°solid | -349.40 ± 1.70 | kJ/mol | NIST |
| ΔfH°solid | -368.60 ± 1.80 | kJ/mol | NIST |
| ΔfusH° | 30.70 | kJ/mol | Solubility of Bisphenol A in Supercritical Carbon Dioxide |
| ΔvapH° | 117.29 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 7.88 | eV | Relay (1.0) Calculated Property |
| log10WS | -2.82 | Aq. Solubility Prediction | |
| logPoct/wat | 3.424 | Crippen Calculated Property | |
| McVol | 186.430 | ml/mol | McGowan Calculated Property |
| Pc | 2937.17 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 7.72e-03 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [359.41; 2108.00] |
|
|
| Inp | 2108.00 | NIST | |
| Inp | 2108.00 | NIST | |
| Inp | 2108.00 | NIST | |
| Inp | 359.41 | NIST | |
| Inp | 2108.00 | NIST | |
| S°solid,1 bar | 287.70 | J/mol×K | NIST |
| Tboil | 633.65 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 849.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [425.65; 431.00] | K |
|
| Tfus | 427.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 425.65 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 427.65 | K | Aq. Solubility Prediction |
| Tfus | 431.00 ± 4.00 | K | NIST |
| Ttriple | [430.15; 433.00] | K |
|
| Ttriple | 430.15 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 433.00 ± 1.00 | K | NIST |
| Ttriple | 433.00 ± 1.00 | K | NIST |
| UQi | 6.50 | ChemSep v8.3 pure component data Compiled value | |
| URi | 8.79 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.677 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2810000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | 287.72 | J/mol×K | 298.15 | NIST |
| ΔfusH | [30.10; 30.10] | kJ/mol | [433.00; 433.00] |
|
| ΔfusH | 30.10 | kJ/mol | 433.00 | NIST |
| ΔfusH | 30.10 | kJ/mol | 433.00 | NIST |
| ΔfusH | 30.10 | kJ/mol | 433.00 | NIST |
| ΔfusH | 30.10 | kJ/mol | 433.00 | NIST |
| ΔvapH | 102.20 | kJ/mol | 550.00 | NIST |
| ΔfusS | [69.60; 69.60] | J/mol×K | [433.00; 433.00] |
|
| ΔfusS | 69.60 | J/mol×K | 433.00 | NIST |
| ΔfusS | 69.60 | J/mol×K | 433.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [493.20; 524.00] | K | [0.50; 1.70] |
|
| Tboilr | 493.20 | K | 0.50 | NIST |
| Tboilr | 524.00 ± 1.00 | K | 1.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [248.13; 685.58] | J/mol×K | [274.00; 1600.15] |
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 | 7.95378e+01 | |||
| Coefficient B | -4.26627e+02 | |||
| Coefficient C | 6.68189e+00 | |||
| Coefficient D | 1.25840e-05 | |||
| Coefficient E | -1.11192e-08 | |||
| Temperature range, min. | 274.00 | |||
| Temperature range, max. | 1600.15 | |||
| Cp,gas | 248.13 | J/mol×K | 274.00 | Calculated Property |
| Cp,gas | 370.36 | J/mol×K | 421.35 | Calculated Property |
| Cp,gas | 457.68 | J/mol×K | 568.70 | Calculated Property |
| Cp,gas | 520.69 | J/mol×K | 716.05 | Calculated Property |
| Cp,gas | 567.55 | J/mol×K | 863.40 | Calculated Property |
| Cp,gas | 603.37 | J/mol×K | 1010.75 | Calculated Property |
| Cp,gas | 631.33 | J/mol×K | 1158.10 | Calculated Property |
| Cp,gas | 653.50 | J/mol×K | 1305.45 | Calculated Property |
| Cp,gas | 671.27 | J/mol×K | 1452.80 | Calculated Property |
| Cp,gas | 685.58 | J/mol×K | 1600.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [541.56; 606.44] | J/mol×K | [455.37; 633.65] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 6.45600e+02 | |||
| Coefficient B | -6.54200e-01 | |||
| Coefficient C | 9.34900e-04 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 455.37 | |||
| Temperature range, max. | 633.65 | |||
| Cp,liquid | 541.56 | J/mol×K | 455.37 | Calculated Property |
| Cp,liquid | 545.83 | J/mol×K | 475.18 | Calculated Property |
| Cp,liquid | 550.84 | J/mol×K | 494.99 | Calculated Property |
| Cp,liquid | 556.58 | J/mol×K | 514.80 | Calculated Property |
| Cp,liquid | 563.06 | J/mol×K | 534.61 | Calculated Property |
| Cp,liquid | 570.27 | J/mol×K | 554.41 | Calculated Property |
| Cp,liquid | 578.21 | J/mol×K | 574.22 | Calculated Property |
| Cp,liquid | 586.89 | J/mol×K | 594.03 | Calculated Property |
| Cp,liquid | 596.30 | J/mol×K | 613.84 | Calculated Property |
| Cp,liquid | 606.44 | J/mol×K | 633.65 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0015228; 0.0001717] | Pa×s | [430.15; 679.20] |
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 | -2.91150e+02 | |||
| Coefficient B | 1.78050e+04 | |||
| Coefficient C | 4.07360e+01 | |||
| Coefficient D | -2.03120e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 430.15 | |||
| Temperature range, max. | 679.20 | |||
| η | 0.0015228 | Pa×s | 430.15 | Calculated Property |
| η | 0.0009601 | Pa×s | 457.82 | Calculated Property |
| η | 0.0006724 | Pa×s | 485.49 | Calculated Property |
| η | 0.0005077 | Pa×s | 513.17 | Calculated Property |
| η | 0.0004042 | Pa×s | 540.84 | Calculated Property |
| η | 0.0003331 | Pa×s | 568.51 | Calculated Property |
| η | 0.0002804 | Pa×s | 596.18 | Calculated Property |
| η | 0.0002384 | Pa×s | 623.86 | Calculated Property |
| η | 0.0002029 | Pa×s | 651.53 | Calculated Property |
| η | 0.0001717 | Pa×s | 679.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [123.29; 0.00] | kJ/mol | [430.15; 849.00] |
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 | 1.95490e+02 | |||
| Coefficient B | 6.52400e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 8.49000e+02 | |||
| Temperature range, min. | 430.15 | |||
| Temperature range, max. | 849.00 | |||
| ΔvapH | 123.29 | kJ/mol | 430.15 | Calculated Property |
| ΔvapH | 114.17 | kJ/mol | 476.69 | Calculated Property |
| ΔvapH | 104.65 | kJ/mol | 523.23 | Calculated Property |
| ΔvapH | 94.64 | kJ/mol | 569.77 | Calculated Property |
| ΔvapH | 84.02 | kJ/mol | 616.31 | Calculated Property |
| ΔvapH | 72.64 | kJ/mol | 662.84 | Calculated Property |
| ΔvapH | 60.21 | kJ/mol | 709.38 | Calculated Property |
| ΔvapH | 46.21 | kJ/mol | 755.92 | Calculated Property |
| ΔvapH | 29.40 | kJ/mol | 802.46 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 849.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [507.33; 665.02] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44248e+01 | |||
| Coefficient B | -4.04412e+03 | |||
| Coefficient C | -2.21266e+02 | |||
| Temperature range, min. | 507.33 | |||
| Temperature range, max. | 665.02 | |||
| Pvap | 1.33 | kPa | 507.33 | Calculated Property |
| Pvap | 3.01 | kPa | 524.85 | Calculated Property |
| Pvap | 6.24 | kPa | 542.37 | Calculated Property |
| Pvap | 11.97 | kPa | 559.89 | Calculated Property |
| Pvap | 21.53 | kPa | 577.41 | Calculated Property |
| Pvap | 36.67 | kPa | 594.94 | Calculated Property |
| Pvap | 59.55 | kPa | 612.46 | Calculated Property |
| Pvap | 92.76 | kPa | 629.98 | Calculated Property |
| Pvap | 139.32 | kPa | 647.50 | Calculated Property |
| Pvap | 202.63 | kPa | 665.02 | Calculated Property |
| Pvap | [7.72e-03; 2976.61] | kPa | [430.15; 849.00] |
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 | 1.94052e+02 | |||
| Coefficient B | -2.47130e+04 | |||
| Coefficient C | -2.33290e+01 | |||
| Coefficient D | 1.03290e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 430.15 | |||
| Temperature range, max. | 849.00 | |||
| Pvap | 7.72e-03 | kPa | 430.15 | Calculated Property |
| Pvap | 0.19 | kPa | 476.69 | Calculated Property |
| Pvap | 2.23 | kPa | 523.23 | Calculated Property |
| Pvap | 14.67 | kPa | 569.77 | Calculated Property |
| Pvap | 63.48 | kPa | 616.31 | Calculated Property |
| Pvap | 200.10 | kPa | 662.84 | Calculated Property |
| Pvap | 495.60 | kPa | 709.38 | Calculated Property |
| Pvap | 1021.75 | kPa | 755.92 | Calculated Property |
| Pvap | 1834.59 | kPa | 802.46 | Calculated Property |
| Pvap | 2976.61 | kPa | 849.00 | Calculated Property |
| Pvap | [4.93e-03; 3034.89] | kPa | [426.15; 849.00] |
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 | 2.95077e+02 | |||
| Coefficient B | -3.04193e+04 | |||
| Coefficient C | -3.80451e+01 | |||
| Coefficient D | 7.42083e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 426.15 | |||
| Temperature range, max. | 849.00 | |||
| Pvap | 4.93e-03 | kPa | 426.15 | Calculated Property |
| Pvap | 0.15 | kPa | 473.13 | Calculated Property |
| Pvap | 1.94 | kPa | 520.12 | Calculated Property |
| Pvap | 13.42 | kPa | 567.10 | Calculated Property |
| Pvap | 59.43 | kPa | 614.08 | Calculated Property |
| Pvap | 189.64 | kPa | 661.07 | Calculated Property |
| Pvap | 475.17 | kPa | 708.05 | Calculated Property |
| Pvap | 995.15 | kPa | 755.03 | Calculated Property |
| Pvap | 1824.84 | kPa | 802.02 | Calculated Property |
| Pvap | 3034.89 | kPa | 849.00 | Calculated Property |
| Pvap | [0.13; 101.42] | kPa | [466.00; 633.70] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.20979e+01 | |||
| Coefficient B | -1.06361e+04 | |||
| Coefficient C | -2.51790e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 466.00 | |||
| Temperature range, max. | 633.70 | |||
| Pvap | 0.13 | kPa | 466.00 | Calculated Property |
| Pvap | 0.35 | kPa | 484.63 | Calculated Property |
| Pvap | 0.86 | kPa | 503.27 | Calculated Property |
| Pvap | 1.98 | kPa | 521.90 | Calculated Property |
| Pvap | 4.30 | kPa | 540.53 | Calculated Property |
| Pvap | 8.84 | kPa | 559.17 | Calculated Property |
| Pvap | 17.31 | kPa | 577.80 | Calculated Property |
| Pvap | 32.43 | kPa | 596.43 | Calculated Property |
| Pvap | 58.39 | kPa | 615.07 | Calculated Property |
| Pvap | 101.42 | kPa | 633.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1059.99; 340.03] | kg/m3 | [430.15; 849.00] |
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 | 8.61324e+01 | |||
| Coefficient B | 2.53310e-01 | |||
| Coefficient C | 8.49000e+02 | |||
| Coefficient D | 2.67100e-01 | |||
| Temperature range, min. | 430.15 | |||
| Temperature range, max. | 849.00 | |||
| ρl | 1059.99 | kg/m3 | 430.15 | Calculated Property |
| ρl | 1023.31 | kg/m3 | 476.69 | Calculated Property |
| ρl | 984.56 | kg/m3 | 523.23 | Calculated Property |
| ρl | 943.23 | kg/m3 | 569.77 | Calculated Property |
| ρl | 898.58 | kg/m3 | 616.31 | Calculated Property |
| ρl | 849.45 | kg/m3 | 662.84 | Calculated Property |
| ρl | 793.83 | kg/m3 | 709.38 | Calculated Property |
| ρl | 727.67 | kg/m3 | 755.92 | Calculated Property |
| ρl | 639.87 | kg/m3 | 802.46 | Calculated Property |
| ρl | 340.03 | kg/m3 | 849.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.01; 0.00] | N/m | [430.15; 849.00] |
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 γ in N/m, T in K | |||
| Coefficient A | 1.87100e-02 | |||
| Coefficient B | 1.15470e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 8.49000e+02 | |||
| Temperature range, min. | 430.15 | |||
| Temperature range, max. | 849.00 | |||
| γ | 0.01 | N/m | 430.15 | Calculated Property |
| γ | 0.01 | N/m | 476.69 | Calculated Property |
| γ | 0.01 | N/m | 523.23 | Calculated Property |
| γ | 0.01 | N/m | 569.77 | Calculated Property |
| γ | 0.00 | N/m | 616.31 | Calculated Property |
| γ | 0.00 | N/m | 662.84 | Calculated Property |
| γ | 0.00 | N/m | 709.38 | Calculated Property |
| γ | 0.00 | N/m | 755.92 | Calculated Property |
| γ | 6.54e-04 | N/m | 802.46 | Calculated Property |
| γ | 0.00 | N/m | 849.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.03; 0.05] | W/m×K | [633.65; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 2.10600e-04 | |||
| Coefficient B | 8.75400e-01 | |||
| Coefficient C | 8.05500e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 633.65 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.03 | W/m×K | 633.65 | Calculated Property |
| λgas | 0.03 | W/m×K | 674.36 | Calculated Property |
| λgas | 0.03 | W/m×K | 715.06 | Calculated Property |
| λgas | 0.03 | W/m×K | 755.77 | Calculated Property |
| λgas | 0.04 | W/m×K | 796.47 | Calculated Property |
| λgas | 0.04 | W/m×K | 837.18 | Calculated Property |
| λgas | 0.04 | W/m×K | 877.88 | Calculated Property |
| λgas | 0.04 | W/m×K | 918.59 | Calculated Property |
| λgas | 0.05 | W/m×K | 959.29 | Calculated Property |
| λgas | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.10] | W/m×K | [430.15; 675.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.30000e-01 | |||
| Coefficient B | -1.98200e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 430.15 | |||
| Temperature range, max. | 675.00 | |||
| λliquid | 0.14 | W/m×K | 430.15 | Calculated Property |
| λliquid | 0.14 | W/m×K | 457.36 | Calculated Property |
| λliquid | 0.13 | W/m×K | 484.56 | Calculated Property |
| λliquid | 0.13 | W/m×K | 511.77 | Calculated Property |
| λliquid | 0.12 | W/m×K | 538.97 | Calculated Property |
| λliquid | 0.12 | W/m×K | 566.18 | Calculated Property |
| λliquid | 0.11 | W/m×K | 593.38 | Calculated Property |
| λliquid | 0.11 | W/m×K | 620.59 | Calculated Property |
| λliquid | 0.10 | W/m×K | 647.79 | Calculated Property |
| λliquid | 0.10 | W/m×K | 675.00 | Calculated Property |
Similar Compounds
![2,2-BIS[(4-TRIMETHYLSILOXY)PHENYL]PROPANE.](data:image/png;base64,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)
![Phenol, 2-[1-(4-hydroxyphenyl)-1-methylethyl]-.](data:image/png;base64,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)
Find more compounds similar to Phenol, 4,4'-(1-methylethylidene)bis-.
Mixtures
- Water + Cetrimonium Bromide + Phenol, 4,4'-(1-methylethylidene)bis-
- Carbon dioxide + Phenol, 4,4'-(1-methylethylidene)bis-
- Water + Phenol, 4,4'-(1-methylethylidene)bis-
- Potassium nitrate + Water + Phenol, 4,4'-(1-methylethylidene)bis-
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
- Aqueous Solubilities of Estrone, 17p-Estradiol, 17a.-Ethynylestradiol, and Bisphenol A
- Solubility of Bisphenol A in Supercritical Carbon Dioxide
- The Solubility Behavior of Bisphenol A in the Presence of Surfactants
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
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