- InChI
- InChI=1S/C12H18/c1-9(2)11-5-7-12(8-6-11)10(3)4/h5-10H,1-4H3
- InChI Key
- SPPWGCYEYAMHDT-UHFFFAOYSA-N
- Formula
- C12H18
- SMILES
- CC(C)c1ccc(C(C)C)cc1
- Molecular Weight1
- 162.27
- CAS
- 100-18-5
- Other Names
-
- 1,4-Bis(1-methylethyl)benzene
- 1,4-diisopropylbenzene
- 4-Isopropylcumene
- Benzene, 1,4-di-(1-methylethyl)
- Benzene, p-diisopropyl-
- benzene, 1,4-diisopropyl-
- p-bis(1-methylethyl)benzene
- p-diisopropylbenzene
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid 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°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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.
- Ip : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (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 | [0.4764; 0.4818] |
|
|
| ω | 0.4818 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.4764 | ChemSep v8.3 pure component data Compiled value | |
| ΔfG° | 147.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -77.60 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°liquid | -132.30 | kJ/mol | NIST |
| ΔfusH° | 13.44 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 56.50 ± 0.30 | kJ/mol | NIST |
| IE | 8.35 | eV | NIST |
| log10WS | -5.20 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.933 | Crippen Calculated Property | |
| McVol | 156.180 | ml/mol | McGowan Calculated Property |
| Pc | [2357.83; 9777.86] | kPa |
|
| Pc | 2360.00 | kPa | Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method |
| Pc | 2357.83 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 2360.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 2358.00 | kPa | KDB |
| Pc | 9777.86 ± 405.30 | kPa | NIST |
| Ptriple | 6.98e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1143.00; 1183.00] |
|
|
| Inp | 1152.70 | NIST | |
| Inp | 1152.10 | NIST | |
| Inp | 1168.70 | NIST | |
| Inp | 1168.90 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1151.20 | NIST | |
| Inp | 1153.40 | NIST | |
| Inp | 1161.60 | NIST | |
| Inp | 1166.70 | NIST | |
| Inp | 1171.30 | NIST | |
| Inp | 1151.20 | NIST | |
| Inp | 1153.40 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1148.55 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1159.50 | NIST | |
| Inp | Outlier 1183.00 | NIST | |
| Inp | 1170.10 | NIST | |
| Inp | 1173.40 | NIST | |
| Inp | 1174.70 | NIST | |
| Inp | 1154.40 | NIST | |
| Inp | 1160.90 | NIST | |
| Inp | 1170.10 | NIST | |
| Inp | 1173.40 | NIST | |
| Inp | 1174.70 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | Outlier 1143.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1161.00 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | 1159.50 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | Outlier 1143.00 | NIST | |
| Ip | [1358.00; 1435.00] |
|
|
| Ip | 1380.70 | NIST | |
| Ip | 1417.60 | NIST | |
| Ip | 1404.00 | NIST | |
| Ip | 1402.00 | NIST | |
| Ip | 1402.00 | NIST | |
| Ip | 1412.00 | NIST | |
| Ip | 1426.00 | NIST | |
| Ip | 1435.00 | NIST | |
| Ip | 1392.00 | NIST | |
| Ip | 1358.00 | NIST | |
| Ip | 1418.00 | NIST | |
| Ip | 1380.70 | NIST | |
| Ip | 1358.00 | NIST | |
| Ip | 1418.00 | NIST | |
| Tboil | [477.00; 483.52] | K |
|
| Tboil | 483.52 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 483.45 | K | KDB |
| Tboil | 483.50 | K | NIST |
| Tboil | 483.52 ± 2.00 | K | NIST |
| Tboil | 483.50 ± 2.00 | K | NIST |
| Tboil | 477.00 ± 8.00 | K | NIST |
| Tboil | 477.65 ± 1.50 | K | NIST |
| Tc | [674.74; 794.15] | K |
|
| Tc | 674.74 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 675.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 674.75 | K | KDB |
| Tc | 794.15 ± 3.00 | K | NIST |
| Tfus | [256.05; 256.15] | K |
|
| Tfus | 256.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 256.08 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 256.05 | K | KDB |
| Tfus | 256.07 ± 0.05 | K | NIST |
| Tfus | 256.11 ± 0.02 | K | NIST |
| Tfus | 256.11 ± 0.02 | K | NIST |
| Tfus | 256.12 ± 0.01 | K | NIST |
| Tfus | 256.08 ± 1.00 | K | NIST |
| Ttriple | 256.08 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 5.69 | ChemSep v8.3 pure component data Compiled value | |
| URi | 7.35 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.584; 0.584] | m3/kmol |
|
| Vc | 0.584 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.584 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.584 | m3/kmol | KDB |
| Zc | [0.2455420; 0.2560000] |
|
|
| Zc | 0.2560000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2455420 | KDB | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [39.30; 56.30] | kJ/mol | [300.50; 448.00] |
|
| ΔvapH | 56.30 ± 0.30 | kJ/mol | 300.50 | NIST |
| ΔvapH | 47.60 | kJ/mol | 439.00 | NIST |
| ΔvapH | 48.90 | kJ/mol | 439.00 | NIST |
| ΔvapH | 50.70 ± 0.20 | kJ/mol | 448.00 | NIST |
| ΔvapH | 46.30 ± 0.30 | kJ/mol | 448.00 | NIST |
| ΔvapH | 43.00 ± 0.50 | kJ/mol | 448.00 | NIST |
| ΔvapH | 39.30 ± 0.90 | kJ/mol | 448.00 | NIST |
| ρl | 860.05 | kg/m3 | 293.10 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [220.80; 595.85] | J/mol×K | [300.00; 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 | 1.00830e+02 | |||
| Coefficient B | -5.31560e+02 | |||
| Coefficient C | 6.54824e+00 | |||
| Coefficient D | 4.33330e-05 | |||
| Coefficient E | -2.41180e-08 | |||
| Temperature range, min. | 300.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 220.80 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 308.47 | J/mol×K | 433.33 | Calculated Property |
| Cp,gas | 378.66 | J/mol×K | 566.67 | Calculated Property |
| Cp,gas | 433.58 | J/mol×K | 700.00 | Calculated Property |
| Cp,gas | 476.88 | J/mol×K | 833.33 | Calculated Property |
| Cp,gas | 511.47 | J/mol×K | 966.67 | Calculated Property |
| Cp,gas | 539.39 | J/mol×K | 1100.00 | Calculated Property |
| Cp,gas | 562.11 | J/mol×K | 1233.33 | Calculated Property |
| Cp,gas | 580.68 | J/mol×K | 1366.67 | Calculated Property |
| Cp,gas | 595.85 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [265.71; 401.55] | J/mol×K | [256.08; 483.65] |
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 | -7.05700e+01 | |||
| Coefficient B | 9.44760e+01 | |||
| Coefficient C | 4.44124e+00 | |||
| Coefficient D | 4.82580e-03 | |||
| Coefficient E | -3.47710e-06 | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 483.65 | |||
| Cp,liquid | 265.71 | J/mol×K | 256.08 | Calculated Property |
| Cp,liquid | 280.00 | J/mol×K | 281.37 | Calculated Property |
| Cp,liquid | 295.27 | J/mol×K | 306.65 | Calculated Property |
| Cp,liquid | 311.12 | J/mol×K | 331.94 | Calculated Property |
| Cp,liquid | 327.21 | J/mol×K | 357.22 | Calculated Property |
| Cp,liquid | 343.24 | J/mol×K | 382.51 | Calculated Property |
| Cp,liquid | 358.93 | J/mol×K | 407.79 | Calculated Property |
| Cp,liquid | 374.04 | J/mol×K | 433.08 | Calculated Property |
| Cp,liquid | 388.32 | J/mol×K | 458.36 | Calculated Property |
| Cp,liquid | 401.55 | J/mol×K | 483.65 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0015610; 0.0001104] | Pa×s | [256.08; 573.00] |
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 | -8.99120e+00 | |||
| Coefficient B | 1.14870e+03 | |||
| Coefficient C | -3.58330e-01 | |||
| Coefficient D | 4.60370e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 573.00 | |||
| η | 0.0015610 | Pa×s | 256.08 | Calculated Property |
| η | 0.0008744 | Pa×s | 291.29 | Calculated Property |
| η | 0.0005541 | Pa×s | 326.51 | Calculated Property |
| η | 0.0003835 | Pa×s | 361.72 | Calculated Property |
| η | 0.0002833 | Pa×s | 396.93 | Calculated Property |
| η | 0.0002200 | Pa×s | 432.15 | Calculated Property |
| η | 0.0001777 | Pa×s | 467.36 | Calculated Property |
| η | 0.0001480 | Pa×s | 502.57 | Calculated Property |
| η | 0.0001265 | Pa×s | 537.79 | Calculated Property |
| η | 0.0001104 | Pa×s | 573.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [59.37; 11.77] | kJ/mol | [256.08; 666.21] |
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 | 9.57210e+01 | |||
| Coefficient B | 2.16614e+00 | |||
| Coefficient C | -4.61607e+00 | |||
| Coefficient D | 4.77725e+00 | |||
| Coefficient E | -1.85237e+00 | |||
| Critical temperature, Tc (K) | 6.75000e+02 | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 666.21 | |||
| ΔvapH | 59.37 | kJ/mol | 256.08 | Calculated Property |
| ΔvapH | 56.44 | kJ/mol | 301.65 | Calculated Property |
| ΔvapH | 53.57 | kJ/mol | 347.22 | Calculated Property |
| ΔvapH | 50.53 | kJ/mol | 392.79 | Calculated Property |
| ΔvapH | 47.14 | kJ/mol | 438.36 | Calculated Property |
| ΔvapH | 43.24 | kJ/mol | 483.93 | Calculated Property |
| ΔvapH | 38.67 | kJ/mol | 529.50 | Calculated Property |
| ΔvapH | 33.13 | kJ/mol | 575.07 | Calculated Property |
| ΔvapH | 25.78 | kJ/mol | 620.64 | Calculated Property |
| ΔvapH | 11.77 | kJ/mol | 666.21 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [358.40; 533.06] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.34508e+01 | |||
| Coefficient B | -3.72488e+03 | |||
| Coefficient C | -7.54240e+01 | |||
| Temperature range, min. | 358.40 | |||
| Temperature range, max. | 533.06 | |||
| Pvap | 1.33 | kPa | 358.40 | Calculated Property |
| Pvap | 3.10 | kPa | 377.81 | Calculated Property |
| Pvap | 6.52 | kPa | 397.21 | Calculated Property |
| Pvap | 12.60 | kPa | 416.62 | Calculated Property |
| Pvap | 22.67 | kPa | 436.03 | Calculated Property |
| Pvap | 38.43 | kPa | 455.43 | Calculated Property |
| Pvap | 61.87 | kPa | 474.84 | Calculated Property |
| Pvap | 95.31 | kPa | 494.25 | Calculated Property |
| Pvap | 141.31 | kPa | 513.65 | Calculated Property |
| Pvap | 202.64 | kPa | 533.06 | Calculated Property |
| Pvap | [6.87e-04; 2360.00] | kPa | [256.08; 654.91] |
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 | 1.14718e+02 | |||
| Coefficient B | -1.07118e+04 | |||
| Coefficient C | -1.45627e+01 | |||
| Coefficient D | 8.94431e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 689 K. | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 654.91 | |||
| Pvap | 6.87e-04 | kPa | 256.08 | Calculated Property |
| Pvap | 0.04 | kPa | 300.39 | Calculated Property |
| Pvap | 0.68 | kPa | 344.71 | Calculated Property |
| Pvap | 5.42 | kPa | 389.02 | Calculated Property |
| Pvap | 26.07 | kPa | 433.34 | Calculated Property |
| Pvap | 89.77 | kPa | 477.65 | Calculated Property |
| Pvap | 246.01 | kPa | 521.97 | Calculated Property |
| Pvap | 575.92 | kPa | 566.28 | Calculated Property |
| Pvap | 1209.63 | kPa | 610.60 | Calculated Property |
| Pvap | 2360.00 | kPa | 654.91 | Calculated Property |
| Pvap | [6.84e-04; 2418.17] | kPa | [256.08; 689.00] |
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 | 8.62940e+01 | |||
| Coefficient B | -9.69497e+03 | |||
| Coefficient C | -1.00850e+01 | |||
| Coefficient D | 3.10925e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 689.00 | |||
| Pvap | 6.84e-04 | kPa | 256.08 | Calculated Property |
| Pvap | 0.05 | kPa | 304.18 | Calculated Property |
| Pvap | 1.02 | kPa | 352.28 | Calculated Property |
| Pvap | 8.54 | kPa | 400.39 | Calculated Property |
| Pvap | 41.44 | kPa | 448.49 | Calculated Property |
| Pvap | 138.67 | kPa | 496.59 | Calculated Property |
| Pvap | 357.64 | kPa | 544.69 | Calculated Property |
| Pvap | 765.46 | kPa | 592.80 | Calculated Property |
| Pvap | 1430.30 | kPa | 640.90 | Calculated Property |
| Pvap | 2418.17 | kPa | 689.00 | Calculated Property |
| Pvap | [3.63; 56.22] | kPa | [393.41; 484.73] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.33955e+01 | |||
| Coefficient B | -3.77956e+03 | |||
| Coefficient C | -8.12040e+01 | |||
| Reference | McDonald, Shrader, et al., 1959, 2 | |||
| Temperature range, min. | 393.41 | |||
| Temperature range, max. | 484.73 | |||
| Pvap | 3.63 | kPa | 393.41 | Calculated Property |
| Pvap | 5.32 | kPa | 403.56 | Calculated Property |
| Pvap | 7.60 | kPa | 413.70 | Calculated Property |
| Pvap | 10.64 | kPa | 423.85 | Calculated Property |
| Pvap | 14.62 | kPa | 434.00 | Calculated Property |
| Pvap | 19.72 | kPa | 444.14 | Calculated Property |
| Pvap | 26.18 | kPa | 454.29 | Calculated Property |
| Pvap | 34.23 | kPa | 464.44 | Calculated Property |
| Pvap | 44.15 | kPa | 474.58 | Calculated Property |
| Pvap | 56.22 | kPa | 484.73 | Calculated Property |
| Pvap | [3.63; 56.22] | kPa | [393.41; 484.73] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.33955e+01 | |||
| Coefficient B | -3.77956e+03 | |||
| Coefficient C | -8.12040e+01 | |||
| Reference | McDonald, Shrader, et al., 1959 | |||
| Temperature range, min. | 393.41 | |||
| Temperature range, max. | 484.73 | |||
| Pvap | 3.63 | kPa | 393.41 | Calculated Property |
| Pvap | 5.32 | kPa | 403.56 | Calculated Property |
| Pvap | 7.60 | kPa | 413.70 | Calculated Property |
| Pvap | 10.64 | kPa | 423.85 | Calculated Property |
| Pvap | 14.62 | kPa | 434.00 | Calculated Property |
| Pvap | 19.72 | kPa | 444.14 | Calculated Property |
| Pvap | 26.18 | kPa | 454.29 | Calculated Property |
| Pvap | 34.23 | kPa | 464.44 | Calculated Property |
| Pvap | 44.15 | kPa | 474.58 | Calculated Property |
| Pvap | 56.22 | kPa | 484.73 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [884.16; 445.36] | kg/m3 | [256.08; 666.21] |
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 | 1.26249e+02 | |||
| Coefficient B | 3.45470e-01 | |||
| Coefficient C | 6.75000e+02 | |||
| Coefficient D | 3.87360e-01 | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 666.21 | |||
| ρl | 884.16 | kg/m3 | 256.08 | Calculated Property |
| ρl | 850.72 | kg/m3 | 301.65 | Calculated Property |
| ρl | 816.10 | kg/m3 | 347.22 | Calculated Property |
| ρl | 779.98 | kg/m3 | 392.79 | Calculated Property |
| ρl | 741.95 | kg/m3 | 438.36 | Calculated Property |
| ρl | 701.32 | kg/m3 | 483.93 | Calculated Property |
| ρl | 656.99 | kg/m3 | 529.50 | Calculated Property |
| ρl | 606.82 | kg/m3 | 575.07 | Calculated Property |
| ρl | 545.49 | kg/m3 | 620.64 | Calculated Property |
| ρl | 445.36 | kg/m3 | 666.21 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 1.67e-05] | N/m | [256.08; 665.39] |
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 | -1.27100e-02 | |||
| Coefficient B | 6.07450e+01 | |||
| Coefficient C | -3.22290e+00 | |||
| Coefficient D | 4.95350e-04 | |||
| Coefficient E | -3.52810e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 666.21 K. | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 665.39 | |||
| γ | 0.03 | N/m | 256.08 | Calculated Property |
| γ | 0.03 | N/m | 301.56 | Calculated Property |
| γ | 0.02 | N/m | 347.04 | Calculated Property |
| γ | 0.02 | N/m | 392.52 | Calculated Property |
| γ | 0.02 | N/m | 438.00 | Calculated Property |
| γ | 0.01 | N/m | 483.47 | Calculated Property |
| γ | 0.01 | N/m | 528.95 | Calculated Property |
| γ | 0.01 | N/m | 574.43 | Calculated Property |
| γ | 0.00 | N/m | 619.91 | Calculated Property |
| γ | 1.67e-05 | N/m | 665.39 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.07] | W/m×K | [256.08; 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 | 3.15960e-01 | |||
| Coefficient B | -7.40420e-02 | |||
| Coefficient C | -3.18590e+02 | |||
| Coefficient D | 1.92860e+06 | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 256.08 | Calculated Property |
| λgas | 0.01 | W/m×K | 338.74 | Calculated Property |
| λgas | 0.02 | W/m×K | 421.40 | Calculated Property |
| λgas | 0.03 | W/m×K | 504.05 | Calculated Property |
| λgas | 0.03 | W/m×K | 586.71 | Calculated Property |
| λgas | 0.04 | W/m×K | 669.37 | Calculated Property |
| λgas | 0.05 | W/m×K | 752.03 | Calculated Property |
| λgas | 0.06 | W/m×K | 834.68 | Calculated Property |
| λgas | 0.06 | W/m×K | 917.34 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.12; 0.08] | W/m×K | [256.08; 483.65] |
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 | -4.34660e-02 | |||
| Coefficient B | -1.47770e+01 | |||
| Coefficient C | -1.47760e+00 | |||
| Coefficient D | -8.00680e-04 | |||
| Coefficient E | -6.90400e-07 | |||
| Temperature range, min. | 256.08 | |||
| Temperature range, max. | 483.65 | |||
| λliquid | 0.12 | W/m×K | 256.08 | Calculated Property |
| λliquid | 0.12 | W/m×K | 281.37 | Calculated Property |
| λliquid | 0.12 | W/m×K | 306.65 | Calculated Property |
| λliquid | 0.11 | W/m×K | 331.94 | Calculated Property |
| λliquid | 0.11 | W/m×K | 357.22 | Calculated Property |
| λliquid | 0.10 | W/m×K | 382.51 | Calculated Property |
| λliquid | 0.10 | W/m×K | 407.79 | Calculated Property |
| λliquid | 0.09 | W/m×K | 433.08 | Calculated Property |
| λliquid | 0.09 | W/m×K | 458.36 | Calculated Property |
| λliquid | 0.08 | W/m×K | 483.65 | Calculated Property |
Similar Compounds
![Ethanone, 1-[4-(1-methylethyl)phenyl]-.](data:image/png;base64,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)
Find more compounds similar to Benzene, 1,4-bis(1-methylethyl)-.
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).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- 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
- Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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