- InChI
- InChI=1S/C18H22O2/c1-17(2,15-11-7-5-8-12-15)19-20-18(3,4)16-13-9-6-10-14-16/h5-14H,1-4H3
- InChI Key
- XMNIXWIUMCBBBL-UHFFFAOYSA-N
- Formula
- C18H22O2
- SMILES
-
CC(C)(OOC(C)(C)c1ccccc1)c1cccc
c1 - Molecular Weight1
- 270.37
- CAS
- 80-43-3
- Other Names
-
- Active dicumyl peroxide
- Bis(1-methyl-1-phenylethyl) peroxide
- Bis(2-phenyl-2-propyl) peroxide
- Bis(«alpha»,«alpha»-dimethylbenzyl) peroxide
- Cumene peroxide
- Cumyl peroxide
- Di-Cup
- Di-Cup 40C
- Di-Cup T
- Di-cup 40haf
- Di-cupr
- Di-«alpha»-cumyl peroxide
- DiCup 40KE
- Dicumene hydroperoxide
- Dicumenyl peroxide
- Diisopropylbenzene peroxide
- Isopropylbenzene peroxide
- Kayacumyl D
- Luperco
- Luperco 500-40C
- Luperco 500-40KE
- Luperox
- Luperox 500
- Luperox 500R
- Luperox 500T
- NSC 56772
- Percumyl D
- Percumyl D 40
- Perkadox B
- Perkadox BC
- Perkadox BC 40
- Perkadox BC 9
- Perkadox BC 95
- Perkadox SB
- Peroxide, bis(1-methyl-1-phenylethyl)
- Peroxide, bis(«alpha»,«alpha»-dimethylbenzyl)
- Peroximon DC-40
- Varox dcp-R
- Varox dcp-T
- «alpha»,«alpha»'-Dicumyl peroxide
- «alpha»-Cumyl peroxide
- ω : Acentric Factor.
- Cp,gas : Ideal gas 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).
- 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).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (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 | 0.4497 | ChemSep v8.3 pure component data Compiled value | |
| ΔfG° | 242.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -79.40 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 18.01 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 92.52 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.30 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.61 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.805 | Crippen Calculated Property | |
| McVol | 228.700 | ml/mol | McGowan Calculated Property |
| Pc | 2180.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 2.05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Tboil | 669.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 884.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [311.15; 313.45] | K |
|
| Tfus | 313.45 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 311.15 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 311.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 8.22 | ChemSep v8.3 pure component data Compiled value | |
| URi | 10.78 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.873 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2590000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | 28.14 | kJ/mol | 312.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [291.05; 857.97] | J/mol×K | [255.00; 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 | 1.52467e+02 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 6.89224e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 291.05 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 428.65 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 536.91 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 619.30 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 682.90 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 733.07 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 773.52 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 806.74 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 834.48 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 857.97 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0217241; 0.0002974] | Pa×s | [300.00; 707.20] |
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 | -1.12820e+01 | |||
| Coefficient B | 2.23580e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 300.00 | |||
| Temperature range, max. | 707.20 | |||
| η | 0.0217241 | Pa×s | 300.00 | Calculated Property |
| η | 0.0081804 | Pa×s | 345.24 | Calculated Property |
| η | 0.0038628 | Pa×s | 390.49 | Calculated Property |
| η | 0.0021316 | Pa×s | 435.73 | Calculated Property |
| η | 0.0013155 | Pa×s | 480.98 | Calculated Property |
| η | 0.0008821 | Pa×s | 526.22 | Calculated Property |
| η | 0.0006301 | Pa×s | 571.47 | Calculated Property |
| η | 0.0004729 | Pa×s | 616.71 | Calculated Property |
| η | 0.0003691 | Pa×s | 661.96 | Calculated Property |
| η | 0.0002974 | Pa×s | 707.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [78.09; 0.00] | kJ/mol | [311.15; 884.00] |
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 | 9.40900e+01 | |||
| Coefficient B | 4.29500e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 8.84000e+02 | |||
| Temperature range, min. | 311.15 | |||
| Temperature range, max. | 884.00 | |||
| ΔvapH | 78.09 | kJ/mol | 311.15 | Calculated Property |
| ΔvapH | 74.24 | kJ/mol | 374.80 | Calculated Property |
| ΔvapH | 70.10 | kJ/mol | 438.45 | Calculated Property |
| ΔvapH | 65.61 | kJ/mol | 502.10 | Calculated Property |
| ΔvapH | 60.67 | kJ/mol | 565.75 | Calculated Property |
| ΔvapH | 55.13 | kJ/mol | 629.40 | Calculated Property |
| ΔvapH | 48.72 | kJ/mol | 693.05 | Calculated Property |
| ΔvapH | 40.93 | kJ/mol | 756.70 | Calculated Property |
| ΔvapH | 30.39 | kJ/mol | 820.35 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 884.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.05; 101.32] | kPa | [311.15; 669.00] |
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 | 4.42322e+01 | |||
| Coefficient B | -3.73160e+03 | |||
| Coefficient C | -5.78000e+00 | |||
| Coefficient D | 5.33230e-03 | |||
| Coefficient E | 1.00000e+00 | |||
| Temperature range, min. | 311.15 | |||
| Temperature range, max. | 669.00 | |||
| Pvap | 2.05 | kPa | 311.15 | Calculated Property |
| Pvap | 4.93 | kPa | 350.91 | Calculated Property |
| Pvap | 9.67 | kPa | 390.67 | Calculated Property |
| Pvap | 16.50 | kPa | 430.43 | Calculated Property |
| Pvap | 25.48 | kPa | 470.19 | Calculated Property |
| Pvap | 36.58 | kPa | 509.96 | Calculated Property |
| Pvap | 49.75 | kPa | 549.72 | Calculated Property |
| Pvap | 64.92 | kPa | 589.48 | Calculated Property |
| Pvap | 82.10 | kPa | 629.24 | Calculated Property |
| Pvap | 101.32 | kPa | 669.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1021.32; 309.63] | kg/m3 | [311.15; 884.00] |
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 | 8.01906e+01 | |||
| Coefficient B | 2.58990e-01 | |||
| Coefficient C | 8.84000e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Temperature range, min. | 311.15 | |||
| Temperature range, max. | 884.00 | |||
| ρl | 1021.32 | kg/m3 | 311.15 | Calculated Property |
| ρl | 981.77 | kg/m3 | 374.80 | Calculated Property |
| ρl | 940.26 | kg/m3 | 438.45 | Calculated Property |
| ρl | 896.32 | kg/m3 | 502.10 | Calculated Property |
| ρl | 849.24 | kg/m3 | 565.75 | Calculated Property |
| ρl | 797.93 | kg/m3 | 629.40 | Calculated Property |
| ρl | 740.50 | kg/m3 | 693.05 | Calculated Property |
| ρl | 673.14 | kg/m3 | 756.70 | Calculated Property |
| ρl | 585.48 | kg/m3 | 820.35 | Calculated Property |
| ρl | 309.63 | kg/m3 | 884.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.01] | N/m | [311.15; 669.00] |
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 | 6.39700e-02 | |||
| Coefficient B | 1.22670e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 8.84000e+02 | |||
| Temperature range, min. | 311.15 | |||
| Temperature range, max. | 669.00 | |||
| γ | 0.04 | N/m | 311.15 | Calculated Property |
| γ | 0.03 | N/m | 350.91 | Calculated Property |
| γ | 0.03 | N/m | 390.67 | Calculated Property |
| γ | 0.03 | N/m | 430.43 | Calculated Property |
| γ | 0.03 | N/m | 470.19 | Calculated Property |
| γ | 0.02 | N/m | 509.96 | Calculated Property |
| γ | 0.02 | N/m | 549.72 | Calculated Property |
| γ | 0.02 | N/m | 589.48 | Calculated Property |
| γ | 0.01 | N/m | 629.24 | Calculated Property |
| γ | 0.01 | N/m | 669.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.09] | W/m×K | [311.15; 669.00] |
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 | 1.99960e-01 | |||
| Coefficient B | -1.63600e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 311.15 | |||
| Temperature range, max. | 669.00 | |||
| λliquid | 0.15 | W/m×K | 311.15 | Calculated Property |
| λliquid | 0.14 | W/m×K | 350.91 | Calculated Property |
| λliquid | 0.14 | W/m×K | 390.67 | Calculated Property |
| λliquid | 0.13 | W/m×K | 430.43 | Calculated Property |
| λliquid | 0.12 | W/m×K | 470.19 | Calculated Property |
| λliquid | 0.12 | W/m×K | 509.96 | Calculated Property |
| λliquid | 0.11 | W/m×K | 549.72 | Calculated Property |
| λliquid | 0.10 | W/m×K | 589.48 | Calculated Property |
| λliquid | 0.10 | W/m×K | 629.24 | Calculated Property |
| λliquid | 0.09 | W/m×K | 669.00 | Calculated Property |
Similar Compounds
![1,1-Dimethyl-1-methyl-1-[(4-methylethyl)phenyl]ethyl peroxide.](data:image/png;base64,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)
Find more compounds similar to Dicumyl peroxide.
Sources
- 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
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
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