Chemical Properties of Benzene, tert-butyl- (CAS 98-06-6)

Benzene, tert-butyl-

InChI
InChI=1S/C10H14/c1-10(2,3)9-7-5-4-6-8-9/h4-8H,1-3H3
InChI Key
YTZKOQUCBOVLHL-UHFFFAOYSA-N
Formula
C10H14
SMILES
CC(C)(C)c1ccccc1
Molecular Weight1
134.22
CAS
98-06-6
Other Names
  • (1,1-dimethylethyl)benzene
  • 1,1-Dimethylethyl-benzene
  • 2-Methyl-2-Phenylpropane
  • 2-Phenyl-2-methylpropane
  • Benzene, (1,1-dimethylethyl)-
  • Benzene, t-butyl-
  • Dimethylethylbenzene
  • NSC 6557
  • Phenyltrimethylmethane
  • Pseudobutylbenzene
  • Trimethylphenylmethane
  • benzene, 1,1-dimethylethyl-
  • t-Butylbenzene
  • tert-butylbenzene
  • «alpha»-dimethylethylbenzene
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Contents

  1. Physical Properties
  2. Temperature Dependent Properties
  3. Datasets
  4. Correlations
  5. Similar Compounds
  6. Mixtures
  7. Sources

Physical Properties

Property Value Unit Source
ω [0.2650; 0.2674]   Show Hide
ω 0.2674 ChemSep v8.3 pure component data
ω 0.2650 KDB
ΔcH°liquid [-5865.20; -5856.76] kJ/mol Show Hide
ΔcH°liquid -5865.20 ± 1.10 kJ/mol NIST
ΔcH°liquid -5856.76 kJ/mol NIST
ΔcH°liquid -5859.60 kJ/mol NIST
μ [0.50; 0.70] debye Show Hide
μ 0.70 debye ChemSep v8.3 pure component data
μ 0.50 debye KDB
ΔfG° 149.95 kJ/mol ChemSep v8.3 pure component data
Δc,grossH 5867.22 kJ/mol KDB
Δc,netH 5559.700 kJ/mol KDB
ΔfH°gas [-22.70; -22.60] kJ/mol Show Hide
ΔfH°gas -22.60 kJ/mol ChemSep v8.3 pure component data
ΔfH°gas -22.69 kJ/mol KDB
ΔfH°gas -22.70 ± 1.40 kJ/mol NIST
ΔfH°liquid -70.80 ± 1.30 kJ/mol NIST
ΔfusH° 8.39 kJ/mol Thermodynamic properties of tert-butylbenzene and 1,4-di-tert-butylbenzene
ΔvapH° [47.50; 49.10] kJ/mol Show Hide
ΔvapH° 47.72 kJ/mol NIST
ΔvapH° 47.50 ± 0.40 kJ/mol NIST
ΔvapH° 47.60 kJ/mol NIST
ΔvapH° 47.70 kJ/mol NIST
ΔvapH° Outlier 49.10 kJ/mol NIST
ΔvapH° 48.10 kJ/mol NIST
IE [8.25; 8.83] eV Show Hide
IE 8.68 ± 0.03 eV NIST
IE 8.69 eV NIST
IE Outlier 8.25 eV NIST
IE 8.63 ± 0.01 eV NIST
IE 8.69 eV NIST
IE 8.72 ± 0.01 eV NIST
IE 8.64 eV NIST
IE 8.68 ± 0.01 eV NIST
IE 8.68 ± 0.01 eV NIST
IE 8.81 eV NIST
IE 8.65 eV NIST
IE 8.74 ± 0.05 eV NIST
IE 8.83 eV NIST
log10WS [-3.66; -3.66]   Show Hide
log10WS -3.66 Aq. Solubility Prediction
log10WS -3.66 Estimated Solubility
logPoct/wat 2.984 Crippen Calculated Property
McVol 128.000 ml/mol McGowan Calculated Property
Pc [2960.00; 2970.00] kPa Show Hide
Pc 2970.00 kPa ChemSep v8.3 pure component data
Pc 2960.00 kPa KDB
Ptriple 9.10e-05 kPa ChemSep v8.3 pure component data
Inp [961.00; 1010.00]   Show Hide
Inp 975.00 NIST
Inp 975.00 NIST
Inp 975.00 NIST
Inp 986.90 NIST
Inp 992.50 NIST
Inp 980.90 NIST
Inp 986.00 NIST
Inp 987.00 NIST
Inp Outlier 1010.00 NIST
Inp Outlier 1008.00 NIST
Inp 986.00 NIST
Inp 988.00 NIST
Inp 986.00 NIST
Inp 987.00 NIST
Inp 982.00 NIST
Inp 974.00 NIST
Inp 971.00 NIST
Inp 974.90 NIST
Inp 975.40 NIST
Inp 980.00 NIST
Inp Outlier 1008.00 NIST
Inp 988.00 NIST
Inp 994.00 NIST
Inp 1001.00 NIST
Inp 969.90 NIST
Inp 972.50 NIST
Inp 987.60 NIST
Inp 993.50 NIST
Inp 1000.90 NIST
Inp 975.00 NIST
Inp 969.90 NIST
Inp 969.90 NIST
Inp 972.50 NIST
Inp 972.00 NIST
Inp 967.08 NIST
Inp 975.40 NIST
Inp 973.30 NIST
Inp 976.00 NIST
Inp 992.00 NIST
Inp 983.22 NIST
Inp 981.00 NIST
Inp 988.00 NIST
Inp 987.10 NIST
Inp 990.50 NIST
Inp 992.00 NIST
Inp 972.40 NIST
Inp 979.30 NIST
Inp 979.10 NIST
Inp 987.10 NIST
Inp 990.50 NIST
Inp 992.00 NIST
Inp 978.00 NIST
Inp 988.00 NIST
Inp 972.82 NIST
Inp 976.53 NIST
Inp 978.96 NIST
Inp 989.31 NIST
Inp 993.20 NIST
Inp 995.68 NIST
Inp 976.00 NIST
Inp 1001.00 NIST
Inp 988.00 NIST
Inp 963.00 NIST
Inp 976.00 NIST
Inp 994.00 NIST
Inp 977.00 NIST
Inp 984.00 NIST
Inp 984.00 NIST
Inp 984.00 NIST
Inp 975.00 NIST
Inp 994.00 NIST
Inp 971.00 NIST
Inp 975.00 NIST
Inp 975.00 NIST
Inp 980.00 NIST
Inp Outlier 961.00 NIST
Inp 988.00 NIST
Inp 973.00 NIST
Inp 986.00 NIST
Inp 991.00 NIST
Inp 986.40 NIST
Inp 993.80 NIST
Inp 991.70 NIST
Inp 991.90 NIST
Inp 973.30 NIST
Inp Outlier 1008.00 NIST
Inp 985.00 NIST
Inp 1000.00 NIST
Inp 971.00 NIST
Inp 981.00 NIST
Inp 972.40 NIST
Inp 992.00 NIST
Inp 978.96 NIST
Inp 976.00 NIST
Inp 1001.00 NIST
Inp 983.22 NIST
I [1215.00; 1287.00]   Show Hide
I 1237.50 NIST
I 1229.50 NIST
I 1215.10 NIST
I 1249.00 NIST
I 1251.00 NIST
I 1262.00 NIST
I 1275.00 NIST
I Outlier 1287.00 NIST
I 1229.00 NIST
I 1239.00 NIST
I 1215.00 NIST
I 1247.00 NIST
I 1215.00 NIST
I 1223.00 NIST
I 1237.50 NIST
S°liquid 278.70 J/mol×K NIST
Tboil [438.00; 443.00] K Show Hide
Tboil 442.30 K ChemSep v8.3 pure component data
Tboil 442.30 K KDB
Tboil 442.30 K NIST
Tboil 441.00 K NIST
Tboil 442.30 ± 0.60 K NIST
Tboil 442.30 ± 0.25 K NIST
Tboil 442.00 ± 2.00 K NIST
Tboil 440.00 ± 2.00 K NIST
Tboil 443.00 ± 3.00 K NIST
Tboil 441.00 ± 6.00 K NIST
Tboil 440.00 ± 3.00 K NIST
Tboil 441.10 ± 0.50 K NIST
Tboil 442.60 ± 0.20 K NIST
Tboil 442.70 ± 0.20 K NIST
Tboil 442.30 ± 0.50 K NIST
Tboil 442.26 ± 0.03 K NIST
Tboil 442.00 ± 2.00 K NIST
Tboil 442.70 ± 0.70 K NIST
Tboil 442.60 ± 0.40 K NIST
Tboil 442.26 ± 0.20 K NIST
Tboil 442.25 ± 0.30 K NIST
Tboil 442.26 ± 0.10 K NIST
Tboil 442.10 ± 0.50 K NIST
Tboil 442.22 ± 0.30 K NIST
Tboil Outlier 439.15 ± 1.00 K NIST
Tboil 442.40 ± 0.40 K NIST
Tboil 441.00 ± 3.00 K NIST
Tboil 442.00 ± 2.00 K NIST
Tboil 442.22 ± 0.50 K NIST
Tboil 442.60 ± 0.30 K NIST
Tboil 442.70 ± 0.30 K NIST
Tboil 442.00 ± 2.00 K NIST
Tboil 442.50 ± 0.40 K NIST
Tboil 441.60 ± 1.50 K NIST
Tboil 442.60 ± 0.30 K NIST
Tboil 442.70 ± 0.30 K NIST
Tboil 442.90 ± 0.20 K NIST
Tboil Outlier 439.00 ± 5.00 K NIST
Tboil 442.20 ± 1.00 K NIST
Tboil 441.00 ± 3.00 K NIST
Tboil Outlier 438.00 ± 5.00 K NIST
Tboil 442.00 ± 3.00 K NIST
Tboil 440.00 ± 3.00 K NIST
Tboil 440.65 ± 2.00 K NIST
Tboil 443.00 ± 2.00 K NIST
Tboil 442.00 ± 3.00 K NIST
Tboil Outlier 439.00 ± 3.00 K NIST
Tboil 440.00 ± 3.00 K NIST
Tboil 442.45 ± 0.50 K NIST
Tboil 441.80 ± 0.30 K NIST
Tc [646.90; 660.00] K Show Hide
Tc 646.90 K DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc 660.00 K ChemSep v8.3 pure component data
Tc 660.00 K KDB
Tfus [212.25; 215.30] K Show Hide
Tfus 215.27 K ChemSep v8.3 pure component data
Tfus 215.30 K KDB
Tfus 214.82 K Aq. Solubility Prediction
Tfus 214.81 ± 0.20 K NIST
Tfus 215.06 ± 0.20 K NIST
Tfus 215.30 ± 0.03 K NIST
Tfus 214.97 ± 0.20 K NIST
Tfus 215.00 ± 2.50 K NIST
Tfus 215.10 ± 1.00 K NIST
Tfus Outlier 212.25 ± 0.40 K NIST
Ttriple [215.00; 215.27] K Show Hide
Ttriple 215.27 K ChemSep v8.3 pure component data
Ttriple 215.00 ± 0.20 K NIST
Ttriple 215.00 ± 0.20 K NIST
UQi 4.58 ChemSep v8.3 pure component data
URi 5.95 ChemSep v8.3 pure component data
Vc 0.460 m3/kmol ChemSep v8.3 pure component data
Zc 0.2660000 ChemSep v8.3 pure component data
Zra 0.27 ChemSep v8.3 pure component data

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid 238.11 J/mol×K 294.30 NIST
Csat [259.00; 293.50] J/mol×K [332.20; 401.30] Show Hide
Csat 259.00 J/mol×K 332.20 Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat 263.10 J/mol×K 342.10 Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat 268.30 J/mol×K 354.90 Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat 272.70 J/mol×K 361.80 Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat 278.40 J/mol×K 371.60 Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat 283.00 J/mol×K 381.50 Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat 288.80 J/mol×K 391.40 Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
Csat 293.50 J/mol×K 401.30 Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
ΔfusH [8.40; 8.41] kJ/mol [215.00; 215.30] Show Hide
ΔfusH 8.41 kJ/mol 215.00 NIST
ΔfusH 8.40 kJ/mol 215.00 NIST
ΔfusH 8.40 kJ/mol 215.00 NIST
ΔfusH 8.40 kJ/mol 215.00 NIST
ΔfusH 8.40 kJ/mol 215.30 NIST
ΔvapH [37.00; 47.80] kJ/mol [293.00; 409.00] Show Hide
ΔvapH 47.80 ± 0.40 kJ/mol 293.00 NIST
ΔvapH 43.70 kJ/mol 400.00 NIST
ΔvapH 43.10 kJ/mol 406.00 NIST
ΔvapH 45.30 ± 0.20 kJ/mol 409.00 NIST
ΔvapH 42.60 ± 0.20 kJ/mol 409.00 NIST
ΔvapH 39.90 ± 0.30 kJ/mol 409.00 NIST
ΔvapH 37.00 ± 0.50 kJ/mol 409.00 NIST
n0 [1.48007; 1.49024]   [298.15; 318.15] Show Hide
n0 1.49003 298.15 Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
n0 1.49009 298.15 Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0 1.49018 298.15 Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0 1.49024 298.15 KDB
n0 1.48763 303.15 Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0 1.48509 308.15 Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0 1.48256 313.15 Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
n0 1.48007 318.15 Volumetric and refractive properties of 1,3,5,7-tetravinyl-1,3,5,7-tetramethylcyclotetrasiloxane with methoxybenzene, chlorobenzene, tert-butylbenzene and nitrobenzene at T = (298.15-318.15) K
ρl [841.72; 867.00] kg/m3 [293.00; 323.15] Show Hide
ρl 867.00 kg/m3 293.00 KDB
ρl 862.23 kg/m3 298.15 Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
ρl 862.28 kg/m3 298.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 854.12 kg/m3 308.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 849.98 kg/m3 313.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 845.87 kg/m3 318.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 841.72 kg/m3 323.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ΔfusS [39.06; 39.06] J/mol×K [215.00; 215.00] Show Hide
ΔfusS 39.06 J/mol×K 215.00 NIST
ΔfusS 39.06 J/mol×K 215.00 NIST

Datasets

  1. Mass density, kg/m3 (1)
  2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 862.38
313.15 100.00 849.98
333.15 100.00 833.32
353.15 100.00 816.42
373.15 100.00 799.33
393.15 100.00 781.81
413.15 100.00 763.74
433.15 100.00 745.23
298.15 20100.00 875.86
313.15 20100.00 864.52
333.15 20100.00 849.54
353.15 20100.00 834.5
373.15 20100.00 819.57
393.15 20100.00 804.5
413.15 20100.00 789.38
433.15 20100.00 774.28
298.15 40100.00 887.54
313.15 40100.00 877.0
333.15 40100.00 863.16
353.15 40100.00 849.4
373.15 40100.00 835.86
393.15 40100.00 822.33
413.15 40100.00 808.84
433.15 40100.00 795.55
298.15 60100.00 897.94
313.15 60100.00 888.01
333.15 60100.00 875.06
353.15 60100.00 862.22
373.15 60100.00 849.64
393.15 60100.00 837.18
413.15 60100.00 824.82
433.15 60100.00 812.75
298.15 80100.00 907.35
313.15 80100.00 897.93
333.15 80100.00 885.65
353.15 80100.00 873.52
373.15 80100.00 861.72
393.15 80100.00 850.05
413.15 80100.00 838.52
433.15 80100.00 827.29
298.15 100100.00 915.98
313.15 100100.00 906.96
333.15 100100.00 895.25
353.15 100100.00 883.72
373.15 100100.00 872.52
393.15 100100.00 861.47
413.15 100100.00 850.58
433.15 100100.00 840.05
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 3 (Liquid)

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Speed of sound, m/s - Liquid
298.15 100.00 1316.4
313.15 100.00 1255.3
333.15 100.00 1176.9
353.15 100.00 1101.8
373.15 100.00 1029.9
393.15 100.00 959.3
413.15 100.00 890.9
433.15 100.00 823.7
298.15 20100.00 1415.8
313.15 20100.00 1360.3
333.15 20100.00 1290.1
353.15 20100.00 1223.5
373.15 20100.00 1161.2
393.15 20100.00 1101.1
413.15 20100.00 1042.6
433.15 20100.00 987.2
298.15 40100.00 1501.7
313.15 40100.00 1450.3
333.15 40100.00 1385.4
353.15 40100.00 1324.4
373.15 40100.00 1267.7
393.15 40100.00 1213.3
413.15 40100.00 1161.1
433.15 40100.00 1112.1
298.15 60100.00 1578.5
313.15 60100.00 1529.8
333.15 60100.00 1469.0
353.15 60100.00 1411.8
373.15 60100.00 1359.0
393.15 60100.00 1308.5
413.15 60100.00 1260.2
433.15 60100.00 1215.1
298.15 80100.00 1647.9
313.15 80100.00 1601.7
333.15 80100.00 1543.9
353.15 80100.00 1489.6
373.15 80100.00 1439.6
393.15 80100.00 1392.0
413.15 80100.00 1346.6
433.15 80100.00 1304.3
298.15 100100.00 1711.7
313.15 100100.00 1667.3
333.15 100100.00 1612.5
353.15 100100.00 1560.2
373.15 100100.00 1512.4
393.15 100100.00 1466.9
413.15 100100.00 1423.8
433.15 100100.00 1383.6
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [132.36; 478.90] J/mol×K [200.00; 1500.00] ChemSep v8.3 pure component data Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A1.13750e+02
Coefficient B-7.76860e+02
Coefficient C6.91724e+00
Coefficient D-5.79700e-04
Coefficient E1.64670e-07
CommentChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 132.36 J/mol×K 200.00 Calculated Property
Cp,gas 202.14 J/mol×K 344.44 Calculated Property
Cp,gas 275.19 J/mol×K 488.89 Calculated Property
Cp,gas 332.85 J/mol×K 633.33 Calculated Property
Cp,gas 375.44 J/mol×K 777.78 Calculated Property
Cp,gas 406.79 J/mol×K 922.22 Calculated Property
Cp,gas 430.45 J/mol×K 1066.67 Calculated Property
Cp,gas 449.13 J/mol×K 1211.11 Calculated Property
Cp,gas 464.80 J/mol×K 1355.56 Calculated Property
Cp,gas 478.90 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [208.04; 253.53] J/mol×K [215.27; 325.00] ChemSep v8.3 pure component data Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.64930e+02
Coefficient B7.01240e+02
Coefficient C-5.72376e+00
Coefficient D3.71220e-02
Coefficient E-3.80060e-05
CommentChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.215.27
Temperature range, max.325.00
Cp,liquid 208.04 J/mol×K 215.27 Calculated Property
Cp,liquid 211.30 J/mol×K 227.46 Calculated Property
Cp,liquid 215.12 J/mol×K 239.65 Calculated Property
Cp,liquid 219.48 J/mol×K 251.85 Calculated Property
Cp,liquid 224.32 J/mol×K 264.04 Calculated Property
Cp,liquid 229.59 J/mol×K 276.23 Calculated Property
Cp,liquid 235.23 J/mol×K 288.42 Calculated Property
Cp,liquid 241.16 J/mol×K 300.62 Calculated Property
Cp,liquid 247.30 J/mol×K 312.81 Calculated Property
Cp,liquid 253.53 J/mol×K 325.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0057592; 0.0001250] Pa×s [215.27; 550.00] ChemSep v8.3 pure component data Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.17000e+01
Coefficient B1.36410e+03
Coefficient C3.87410e-02
Coefficient D-3.80130e-08
Coefficient E2.00000e+00
CommentChemSep eq 101, LiquidViscosity
Temperature range, min.215.27
Temperature range, max.550.00
η 0.0057592 Pa×s 215.27 Calculated Property
η 0.0022769 Pa×s 252.46 Calculated Property
η 0.0011429 Pa×s 289.65 Calculated Property
η 0.0006713 Pa×s 326.85 Calculated Property
η 0.0004397 Pa×s 364.04 Calculated Property
η 0.0003115 Pa×s 401.23 Calculated Property
η 0.0002340 Pa×s 438.42 Calculated Property
η 0.0001838 Pa×s 475.62 Calculated Property
η 0.0001495 Pa×s 512.81 Calculated Property
η 0.0001250 Pa×s 550.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [52.83; 0.00] kJ/mol [215.27; 660.00] ChemSep v8.3 pure component data Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A6.31670e+01
Coefficient B4.52620e-01
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Critical temperature, Tc (K)6.60000e+02
CommentChemSep eq 106, HeatOfVaporization
Temperature range, min.215.27
Temperature range, max.660.00
ΔvapH 52.83 kJ/mol 215.27 Calculated Property
ΔvapH 50.09 kJ/mol 264.68 Calculated Property
ΔvapH 47.15 kJ/mol 314.10 Calculated Property
ΔvapH 43.97 kJ/mol 363.51 Calculated Property
ΔvapH 40.49 kJ/mol 412.93 Calculated Property
ΔvapH 36.60 kJ/mol 462.34 Calculated Property
ΔvapH 32.13 kJ/mol 511.76 Calculated Property
ΔvapH 26.74 kJ/mol 561.17 Calculated Property
ΔvapH 19.54 kJ/mol 610.59 Calculated Property
ΔvapH 0.00 kJ/mol 660.00 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.63] kPa [321.92; 472.91] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.38431e+01
Coefficient B-3.47592e+03
Coefficient C-6.54960e+01
Temperature range, min.321.92
Temperature range, max.472.91
Pvap 1.33 kPa 321.92 Calculated Property
Pvap 3.07 kPa 338.70 Calculated Property
Pvap 6.40 kPa 355.47 Calculated Property
Pvap 12.33 kPa 372.25 Calculated Property
Pvap 22.18 kPa 389.03 Calculated Property
Pvap 37.68 kPa 405.80 Calculated Property
Pvap 60.88 kPa 422.58 Calculated Property
Pvap 94.23 kPa 439.36 Calculated Property
Pvap 140.47 kPa 456.13 Calculated Property
Pvap 202.63 kPa 472.91 Calculated Property
Pvap [1.18e-04; 2977.57] kPa [215.27; 660.00] ChemSep v8.3 pure component data Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A8.06662e+01
Coefficient B-8.35220e+03
Coefficient C-9.51180e+00
Coefficient D3.99530e-06
Coefficient E2.00000e+00
CommentChemSep eq 101, VaporPressure
Temperature range, min.215.27
Temperature range, max.660.00
Pvap 1.18e-04 kPa 215.27 Calculated Property
Pvap 0.03 kPa 264.68 Calculated Property
Pvap 0.80 kPa 314.10 Calculated Property
Pvap 8.48 kPa 363.51 Calculated Property
Pvap 46.00 kPa 412.93 Calculated Property
Pvap 162.07 kPa 462.34 Calculated Property
Pvap 427.85 kPa 511.76 Calculated Property
Pvap 926.08 kPa 561.17 Calculated Property
Pvap 1744.26 kPa 610.59 Calculated Property
Pvap 2977.57 kPa 660.00 Calculated Property
Pvap [8.71e-05; 2953.38] kPa [215.27; 660.00] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A9.26802e+01
Coefficient B-8.94559e+03
Coefficient C-1.13016e+01
Coefficient D5.13608e-06
Coefficient E0.00000e+00
Temperature range, min.215.27
Temperature range, max.660.00
Pvap 8.71e-05 kPa 215.27 Calculated Property
Pvap 0.02 kPa 264.68 Calculated Property
Pvap 0.76 kPa 314.10 Calculated Property
Pvap 8.31 kPa 363.51 Calculated Property
Pvap 45.58 kPa 412.93 Calculated Property
Pvap 160.69 kPa 462.34 Calculated Property
Pvap 422.98 kPa 511.76 Calculated Property
Pvap 913.35 kPa 561.17 Calculated Property
Pvap 1721.29 kPa 610.59 Calculated Property
Pvap 2953.38 kPa 660.00 Calculated Property
Pvap [6.41; 103.98] kPa [357.03; 443.31] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.39200e+01
Coefficient B-3.46441e+03
Coefficient C-6.98220e+01
ReferenceForziati, Norris, et al., 1949, 2
Temperature range, min.357.03
Temperature range, max.443.31
Pvap 6.41 kPa 357.03 Calculated Property
Pvap 9.46 kPa 366.62 Calculated Property
Pvap 13.63 kPa 376.20 Calculated Property
Pvap 19.21 kPa 385.79 Calculated Property
Pvap 26.54 kPa 395.38 Calculated Property
Pvap 35.98 kPa 404.96 Calculated Property
Pvap 47.96 kPa 414.55 Calculated Property
Pvap 62.95 kPa 424.14 Calculated Property
Pvap 81.44 kPa 433.72 Calculated Property
Pvap 103.98 kPa 443.31 Calculated Property
Pvap [6.41; 103.98] kPa [357.03; 443.31] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.39200e+01
Coefficient B-3.46441e+03
Coefficient C-6.98220e+01
ReferenceForziati, Norris, et al., 1949
Temperature range, min.357.03
Temperature range, max.443.31
Pvap 6.41 kPa 357.03 Calculated Property
Pvap 9.46 kPa 366.62 Calculated Property
Pvap 13.63 kPa 376.20 Calculated Property
Pvap 19.21 kPa 385.79 Calculated Property
Pvap 26.54 kPa 395.38 Calculated Property
Pvap 35.98 kPa 404.96 Calculated Property
Pvap 47.96 kPa 414.55 Calculated Property
Pvap 62.95 kPa 424.14 Calculated Property
Pvap 81.44 kPa 433.72 Calculated Property
Pvap 103.98 kPa 443.31 Calculated Property
Property Value Unit Temperature (K) Source
ρl [929.69; 272.80] kg/m3 [215.27; 660.00] ChemSep v8.3 pure component data Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A6.83936e+01
Coefficient B2.50710e-01
Coefficient C6.60000e+02
Coefficient D3.05840e-01
CommentChemSep eq 105, LiquidDensity
Temperature range, min.215.27
Temperature range, max.660.00
ρl 929.69 kg/m3 215.27 Calculated Property
ρl 890.22 kg/m3 264.68 Calculated Property
ρl 849.07 kg/m3 314.10 Calculated Property
ρl 805.81 kg/m3 363.51 Calculated Property
ρl 759.84 kg/m3 412.93 Calculated Property
ρl 710.19 kg/m3 462.34 Calculated Property
ρl 655.20 kg/m3 511.76 Calculated Property
ρl 591.56 kg/m3 561.17 Calculated Property
ρl 510.25 kg/m3 610.59 Calculated Property
ρl 272.80 kg/m3 660.00 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 8.07e-06] N/m [215.27; 654.66] ChemSep v8.3 pure component data Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-6.56590e-03
Coefficient B7.40350e+01
Coefficient C-3.54010e+00
Coefficient D1.52400e-03
Coefficient E-6.05560e-06
CommentChemSep eq 16, SurfaceTension, ChemSep Tmax 660 K
Temperature range, min.215.27
Temperature range, max.654.66
γ 0.04 N/m 215.27 Calculated Property
γ 0.03 N/m 264.09 Calculated Property
γ 0.03 N/m 312.91 Calculated Property
γ 0.02 N/m 361.73 Calculated Property
γ 0.02 N/m 410.56 Calculated Property
γ 0.01 N/m 459.38 Calculated Property
γ 0.01 N/m 508.20 Calculated Property
γ 0.01 N/m 557.02 Calculated Property
γ 0.00 N/m 605.84 Calculated Property
γ 8.07e-06 N/m 654.66 Calculated Property
Property Value Unit Temperature (K) Source
λ [0.01; 0.08] W/m×K [215.27; 1000.00] ChemSep v8.3 pure component data Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λ in W/m×K, T in K
Coefficient A1.89550e-05
Coefficient B1.22910e+00
Coefficient C1.30740e+02
Coefficient D5.33490e+04
CommentChemSep eq 102, VaporThermalConductivity
Temperature range, min.215.27
Temperature range, max.1000.00
λ 0.01 W/m×K 215.27 Calculated Property
λ 0.01 W/m×K 302.46 Calculated Property
λ 0.02 W/m×K 389.65 Calculated Property
λ 0.02 W/m×K 476.85 Calculated Property
λ 0.03 W/m×K 564.04 Calculated Property
λ 0.04 W/m×K 651.23 Calculated Property
λ 0.05 W/m×K 738.42 Calculated Property
λ 0.06 W/m×K 825.62 Calculated Property
λ 0.07 W/m×K 912.81 Calculated Property
λ 0.08 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λ [0.13; 0.10] W/m×K [215.27; 442.30] ChemSep v8.3 pure component data Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λ in W/m×K, T in K
Coefficient A5.20230e-02
Coefficient B-1.43300e+02
Coefficient C-6.96730e-01
Coefficient D-5.73330e-03
Coefficient E2.26270e-06
CommentChemSep eq 16, LiquidThermalConductivity
Temperature range, min.215.27
Temperature range, max.442.30
λ 0.13 W/m×K 215.27 Calculated Property
λ 0.13 W/m×K 240.50 Calculated Property
λ 0.13 W/m×K 265.72 Calculated Property
λ 0.12 W/m×K 290.95 Calculated Property
λ 0.12 W/m×K 316.17 Calculated Property
λ 0.11 W/m×K 341.40 Calculated Property
λ 0.11 W/m×K 366.62 Calculated Property
λ 0.10 W/m×K 391.85 Calculated Property
λ 0.10 W/m×K 417.07 Calculated Property
λ 0.10 W/m×K 442.30 Calculated Property

Similar Compounds

1,4-Ditertiary butylbenzene. Benzene, 1,3-bis(1,1-dimethylethyl)-. Naphthalene, 2-(1,1-dimethylethyl)-. 4-t-Butylbenzonitrile. Anthracene, 2-(1,1-dimethylethyl)-. 1-Chloro-4-(1,1-dimethylethyl)benzene. Naphthalene, 2,6-bis(1,1-dimethylethyl)-. Benzene, 1-bromo-4-(1,1-dimethylethyl)-. 3-TERT.-BUTYLBROMOBENZENE. 1-CHLORO-2-METHYL-2-PHENYLPROPANE. m-Tert-butyl chlorobenzene. Naphthalene, 1-(1,1-dimethylethyl)-. 4-tert-Butyltoluene. Phenanthrene, 3,9-bis(1,1-dimethylethyl)-. Benzene, 1,3,5-tris(1,1-dimethylethyl)-.

Find more compounds similar to Benzene, tert-butyl-.

Mixtures

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