Chemical Properties of Benzene, 1,2,3,4-tetramethyl- (CAS 488-23-3)

Benzene, 1,2,3,4-tetramethyl-

InChI
InChI=1S/C10H14/c1-7-5-6-8(2)10(4)9(7)3/h5-6H,1-4H3
InChI Key
UOHMMEJUHBCKEE-UHFFFAOYSA-N
Formula
C10H14
SMILES
Cc1ccc(C)c(C)c1C
Molecular Weight1
134.22
CAS
488-23-3
Other Names
  • 1,2,3,4-Tetramethylbenzene
  • Prehnitene
  • Prehnitol
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Physical Properties

Property Value Unit Source
ω [0.3879; 0.4172]   Show Hide
ω 0.3879 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.4172 ChemSep v8.3 pure component data Compiled value
ΔcH°liquid [-5845.70; -5827.50] kJ/mol Show Hide
ΔcH°liquid -5845.70 ± 1.10 kJ/mol NIST
ΔcH°liquid -5839.60 ± 3.00 kJ/mol NIST
ΔcH°liquid -5827.50 ± 5.90 kJ/mol NIST
μ 0.50 debye ChemSep v8.3 pure component data Compiled value
ΔfG° 132.40 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas [-43.80; -33.05] kJ/mol Show Hide
ΔfH°gas -33.05 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -36.00 ± 1.40 kJ/mol NIST
ΔfH°gas -37.60 ± 1.20 kJ/mol NIST
ΔfH°gas -43.80 ± 3.00 kJ/mol NIST
ΔfH°liquid [-96.40; -90.20] kJ/mol Show Hide
ΔfH°liquid -90.20 ± 1.20 kJ/mol NIST
ΔfH°liquid -96.40 ± 3.00 kJ/mol NIST
ΔfusH° 14.53 kJ/mol Joback Calculated Property
ΔvapH° [52.56; 57.20] kJ/mol Show Hide
ΔvapH° 54.00 kJ/mol NIST
ΔvapH° 52.56 ± 0.17 kJ/mol NIST
ΔvapH° 52.60 ± 0.20 kJ/mol NIST
ΔvapH° 57.20 kJ/mol NIST
IE [8.14; 8.18] eV Show Hide
IE 8.14 eV NIST
IE 8.18 eV NIST
IE 8.14 eV NIST
log10WS -3.95 Relay (1.0) Calculated Property
logPoct/wat 2.920 Crippen Calculated Property
McVol 128.000 ml/mol McGowan Calculated Property
Pc [2860.00; 3273.81] kPa Show Hide
Pc 3273.81 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 2860.00 kPa ChemSep v8.3 pure component data Compiled value
Ptriple 2.99e-03 kPa ChemSep v8.3 pure component data Compiled value
Inp [1120.00; 1187.00]   Show Hide
Inp 1150.40 NIST
Inp 1159.80 NIST
Inp Outlier 1169.40 NIST
Inp 1140.90 NIST
Inp 1139.00 NIST
Inp 1139.00 NIST
Inp 1139.00 NIST
Inp 1136.00 NIST
Inp 1127.50 NIST
Inp 1129.20 NIST
Inp 1132.70 NIST
Inp 1135.00 NIST
Inp 1129.20 NIST
Inp 1132.70 NIST
Inp 1139.00 NIST
Inp 1125.98 NIST
Inp 1160.00 NIST
Inp 1165.00 NIST
Inp 1168.00 NIST
Inp 1136.00 NIST
Inp 1125.60 NIST
Inp 1150.40 NIST
Inp 1133.00 NIST
Inp Outlier 1187.00 NIST
Inp 1147.00 NIST
Inp 1142.00 NIST
Inp 1120.00 NIST
Inp 1122.00 NIST
Inp 1145.30 NIST
Inp 1149.90 NIST
Inp 1148.20 NIST
Inp 1144.20 NIST
Inp 1153.80 NIST
Inp Outlier 1175.20 NIST
Inp 1144.20 NIST
Inp 1149.90 NIST
Inp 1153.80 NIST
Inp 1148.20 NIST
Inp 1135.84 NIST
Inp 1136.00 NIST
Inp 1133.00 NIST
Inp 1144.00 NIST
Inp 1142.00 NIST
Inp 1127.00 NIST
Inp 1142.00 NIST
Inp 1142.00 NIST
Inp 1148.00 NIST
Inp 1147.00 NIST
Inp 1162.00 NIST
Inp 1151.00 NIST
Inp 1153.00 NIST
Inp 1149.00 NIST
Inp 1144.00 NIST
Inp 1161.40 NIST
Inp 1130.00 NIST
Inp 1132.00 NIST
Inp 1145.00 NIST
Inp 1151.00 NIST
Inp 1128.00 NIST
Inp 1128.00 NIST
Inp 1131.00 NIST
Inp 1135.00 NIST
Inp 1138.00 NIST
Inp 1125.00 NIST
Inp 1148.00 NIST
Inp 1149.00 NIST
Inp 1144.00 NIST
Inp 1147.00 NIST
Inp 1145.00 NIST
Inp 1135.00 NIST
Inp 1159.80 NIST
Inp 1139.00 NIST
Inp 1132.70 NIST
Inp 1125.98 NIST
Inp 1125.60 NIST
Ip [1430.00; 1505.10]   Show Hide
Ip 1505.10 NIST
Ip 1461.60 NIST
Ip 1456.00 NIST
Ip 1434.70 NIST
Ip 1436.00 NIST
Ip 1430.00 NIST
Ip 1493.00 NIST
Ip 1495.00 NIST
Ip 1435.00 NIST
Ip 1462.00 NIST
Ip 1464.00 NIST
Ip 1476.00 NIST
Ip 1462.00 NIST
Ip 1462.00 NIST
Ip 1505.10 NIST
S°liquid 290.80 J/mol×K NIST
Tboil [477.00; 478.40] K Show Hide
Tboil 478.19 K ChemSep v8.3 pure component data Compiled value
Tboil 478.20 K NIST
Tboil 478.15 ± 0.50 K NIST
Tboil 477.98 ± 0.30 K NIST
Tboil 478.30 ± 0.50 K NIST
Tboil 478.25 ± 0.30 K NIST
Tboil 478.40 ± 1.00 K NIST
Tboil 478.19 ± 0.30 K NIST
Tboil Outlier 477.00 ± 3.00 K NIST
Tc [690.00; 700.50] K Show Hide
Tc 700.50 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 690.00 K ChemSep v8.3 pure component data Compiled value
Tfus [265.50; 267.05] K Show Hide
Tfus 267.05 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 266.90 K ChemSep v8.3 pure component data Compiled value
Tfus 266.82 ± 0.20 K NIST
Tfus 265.50 ± 1.00 K NIST
Tfus 265.75 ± 2.50 K NIST
Tfus 266.75 ± 0.10 K NIST
Ttriple [265.40; 266.90] K Show Hide
Ttriple 266.90 K ChemSep v8.3 pure component data Compiled value
Ttriple 265.40 ± 0.30 K NIST
Ttriple 265.40 ± 0.30 K NIST
UQi 4.67 ChemSep v8.3 pure component data Compiled value
URi 6.13 ChemSep v8.3 pure component data Compiled value
Vc [0.436; 0.482] m3/kmol Show Hide
Vc 0.436 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.482 m3/kmol ChemSep v8.3 pure component data Compiled value
Zc 0.2560000 ChemSep v8.3 pure component data Compiled value
Zra 0.26 ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [233.00; 291.00] J/mol×K [280.00; 380.00] Show Hide
Cp,liquid 233.00 J/mol×K 280.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 238.00 J/mol×K 290.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 236.00 J/mol×K 291.90 NIST
Cp,liquid 244.30 J/mol×K 298.00 NIST
Cp,liquid 243.00 J/mol×K 298.15 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 244.00 J/mol×K 300.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 250.00 J/mol×K 310.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 256.00 J/mol×K 320.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 262.00 J/mol×K 330.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 267.00 J/mol×K 340.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 273.00 J/mol×K 350.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 279.00 J/mol×K 360.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 285.00 J/mol×K 370.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 291.00 J/mol×K 380.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH [11.23; 11.23] kJ/mol [265.40; 265.40] Show Hide
ΔfusH 11.23 kJ/mol 265.40 NIST
ΔfusH 11.23 kJ/mol 265.40 NIST
ΔfusH 11.23 kJ/mol 265.40 NIST
ΔfusH 11.23 kJ/mol 265.40 NIST
ΔvapH [50.70; 55.70] kJ/mol [396.50; 430.50] Show Hide
ΔvapH 55.70 kJ/mol 396.50 NIST
ΔvapH 50.70 kJ/mol 430.50 NIST
ΔfusS [42.30; 42.30] J/mol×K [265.40; 265.40] Show Hide
ΔfusS 42.30 J/mol×K 265.40 NIST
ΔfusS 42.30 J/mol×K 265.40 NIST

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [140.72; 477.43] J/mol×K [200.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A1.08680e+02
Coefficient B-5.36060e+02
Coefficient C6.09824e+00
Coefficient D2.65780e-04
Coefficient E-1.01970e-07
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 140.72 J/mol×K 200.00 Calculated Property
Cp,gas 210.32 J/mol×K 344.44 Calculated Property
Cp,gas 273.91 J/mol×K 488.89 Calculated Property
Cp,gas 325.54 J/mol×K 633.33 Calculated Property
Cp,gas 366.96 J/mol×K 777.78 Calculated Property
Cp,gas 400.27 J/mol×K 922.22 Calculated Property
Cp,gas 427.04 J/mol×K 1066.67 Calculated Property
Cp,gas 448.34 J/mol×K 1211.11 Calculated Property
Cp,gas 464.95 J/mol×K 1355.56 Calculated Property
Cp,gas 477.43 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [229.36; 376.68] J/mol×K [266.90; 519.75] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.91090e+02
Coefficient B-1.52770e+03
Coefficient C1.33232e+01
Coefficient D-1.99770e-02
Coefficient E1.93330e-05
Temperature range, min.266.90
Temperature range, max.519.75
Cp,liquid 229.36 J/mol×K 266.90 Calculated Property
Cp,liquid 242.19 J/mol×K 294.99 Calculated Property
Cp,liquid 255.07 J/mol×K 323.09 Calculated Property
Cp,liquid 267.94 J/mol×K 351.18 Calculated Property
Cp,liquid 281.07 J/mol×K 379.28 Calculated Property
Cp,liquid 294.99 J/mol×K 407.37 Calculated Property
Cp,liquid 310.42 J/mol×K 435.47 Calculated Property
Cp,liquid 328.31 J/mol×K 463.56 Calculated Property
Cp,liquid 349.86 J/mol×K 491.66 Calculated Property
Cp,liquid 376.68 J/mol×K 519.75 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0031742; 0.0000848] Pa×s [266.90; 573.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.25550e+01
Coefficient B1.81080e+03
Coefficient C3.21120e-03
Coefficient D-3.01990e-09
Coefficient E2.00000e+00
Temperature range, min.266.90
Temperature range, max.573.00
η 0.0031742 Pa×s 266.90 Calculated Property
η 0.0014748 Pa×s 300.91 Calculated Property
η 0.0008007 Pa×s 334.92 Calculated Property
η 0.0004865 Pa×s 368.93 Calculated Property
η 0.0003216 Pa×s 402.94 Calculated Property
η 0.0002267 Pa×s 436.96 Calculated Property
η 0.0001681 Pa×s 470.97 Calculated Property
η 0.0001298 Pa×s 504.98 Calculated Property
η 0.0001035 Pa×s 538.99 Calculated Property
η 0.0000848 Pa×s 573.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [57.71; 20.95] kJ/mol [266.90; 670.57] ChemSep v8.3 pure component data Compiled value 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 A6.82774e+01
Coefficient B2.06590e-01
Coefficient C3.54625e-01
Coefficient D1.56354e-01
Coefficient E-4.00825e-01
Critical temperature, Tc (K)6.90000e+02
Temperature range, min.266.90
Temperature range, max.670.57
ΔvapH 57.71 kJ/mol 266.90 Calculated Property
ΔvapH 54.93 kJ/mol 311.75 Calculated Property
ΔvapH 51.93 kJ/mol 356.60 Calculated Property
ΔvapH 48.73 kJ/mol 401.46 Calculated Property
ΔvapH 45.36 kJ/mol 446.31 Calculated Property
ΔvapH 41.84 kJ/mol 491.16 Calculated Property
ΔvapH 38.12 kJ/mol 536.01 Calculated Property
ΔvapH 34.08 kJ/mol 580.87 Calculated Property
ΔvapH 29.20 kJ/mol 625.72 Calculated Property
ΔvapH 20.95 kJ/mol 670.57 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [353.60; 508.82] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.46818e+01
Coefficient B-4.16744e+03
Coefficient C-6.40760e+01
Temperature range, min.353.60
Temperature range, max.508.82
Pvap 1.33 kPa 353.60 Calculated Property
Pvap 3.00 kPa 370.85 Calculated Property
Pvap 6.17 kPa 388.09 Calculated Property
Pvap 11.82 kPa 405.34 Calculated Property
Pvap 21.27 kPa 422.59 Calculated Property
Pvap 36.27 kPa 439.83 Calculated Property
Pvap 59.01 kPa 457.08 Calculated Property
Pvap 92.16 kPa 474.33 Calculated Property
Pvap 138.85 kPa 491.57 Calculated Property
Pvap 202.64 kPa 508.82 Calculated Property
Pvap [3.28e-03; 2949.92] kPa [266.90; 690.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A9.64860e+01
Coefficient B-9.86660e+03
Coefficient C-1.17465e+01
Coefficient D5.43265e-06
Coefficient E2.00000e+00
CommentRange stopped at Tc; ChemSep gives it to 693 K.
Temperature range, min.266.90
Temperature range, max.690.00
Pvap 3.28e-03 kPa 266.90 Calculated Property
Pvap 0.14 kPa 313.91 Calculated Property
Pvap 1.98 kPa 360.92 Calculated Property
Pvap 13.38 kPa 407.93 Calculated Property
Pvap 56.38 kPa 454.94 Calculated Property
Pvap 172.86 kPa 501.96 Calculated Property
Pvap 425.19 kPa 548.97 Calculated Property
Pvap 895.61 kPa 595.98 Calculated Property
Pvap 1690.03 kPa 642.99 Calculated Property
Pvap 2949.92 kPa 690.00 Calculated Property
Pvap [1.30; 2832.30] kPa [352.15; 695.10] 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 A9.69035e+01
Coefficient B-9.94657e+03
Coefficient C-1.17674e+01
Coefficient D4.88689e-06
Coefficient E0.00000e+00
Temperature range, min.352.15
Temperature range, max.695.10
Pvap 1.30 kPa 352.15 Calculated Property
Pvap 7.01 kPa 390.26 Calculated Property
Pvap 26.32 kPa 428.36 Calculated Property
Pvap 76.02 kPa 466.47 Calculated Property
Pvap 180.93 kPa 504.57 Calculated Property
Pvap 372.64 kPa 542.68 Calculated Property
Pvap 688.03 kPa 580.78 Calculated Property
Pvap 1169.00 kPa 618.89 Calculated Property
Pvap 1864.14 kPa 656.99 Calculated Property
Pvap 2832.30 kPa 695.10 Calculated Property
Pvap [0.13; 101.49] kPa [315.80; 477.60] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.43128e+01
Coefficient B-3.85723e+03
Coefficient C-7.96550e+01
ReferenceStull, 1947
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.315.80
Temperature range, max.477.60
Pvap 0.13 kPa 315.80 Calculated Property
Pvap 0.42 kPa 333.78 Calculated Property
Pvap 1.15 kPa 351.76 Calculated Property
Pvap 2.76 kPa 369.73 Calculated Property
Pvap 6.00 kPa 387.71 Calculated Property
Pvap 11.97 kPa 405.69 Calculated Property
Pvap 22.20 kPa 423.67 Calculated Property
Pvap 38.75 kPa 441.64 Calculated Property
Pvap 64.16 kPa 459.62 Calculated Property
Pvap 101.49 kPa 477.60 Calculated Property
Property Value Unit Temperature (K) Source
ρl [923.80; 470.07] kg/m3 [266.90; 670.57] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A8.41159e+01
Coefficient B2.76000e-01
Coefficient C6.90000e+02
Coefficient D3.05010e-01
Temperature range, min.266.90
Temperature range, max.670.57
ρl 923.80 kg/m3 266.90 Calculated Property
ρl 890.01 kg/m3 311.75 Calculated Property
ρl 854.71 kg/m3 356.60 Calculated Property
ρl 817.54 kg/m3 401.46 Calculated Property
ρl 778.02 kg/m3 446.31 Calculated Property
ρl 735.37 kg/m3 491.16 Calculated Property
ρl 688.35 kg/m3 536.01 Calculated Property
ρl 634.66 kg/m3 580.87 Calculated Property
ρl 568.91 kg/m3 625.72 Calculated Property
ρl 470.07 kg/m3 670.57 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 8.32e-04] N/m [266.90; 670.57] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-9.78070e-03
Coefficient B2.01260e+02
Coefficient C-4.27690e+00
Coefficient D3.75720e-03
Coefficient E-6.86820e-06
Temperature range, min.266.90
Temperature range, max.670.57
γ 0.04 N/m 266.90 Calculated Property
γ 0.03 N/m 311.75 Calculated Property
γ 0.03 N/m 356.60 Calculated Property
γ 0.02 N/m 401.46 Calculated Property
γ 0.02 N/m 446.31 Calculated Property
γ 0.02 N/m 491.16 Calculated Property
γ 0.01 N/m 536.01 Calculated Property
γ 0.01 N/m 580.87 Calculated Property
γ 0.00 N/m 625.72 Calculated Property
γ 8.32e-04 N/m 670.57 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.08] W/m×K [266.90; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A1.00100e-04
Coefficient B1.03310e+00
Coefficient C6.53920e+02
Coefficient D2.14660e+04
Temperature range, min.266.90
Temperature range, max.1000.00
λgas 0.01 W/m×K 266.90 Calculated Property
λgas 0.01 W/m×K 348.36 Calculated Property
λgas 0.02 W/m×K 429.81 Calculated Property
λgas 0.03 W/m×K 511.27 Calculated Property
λgas 0.03 W/m×K 592.72 Calculated Property
λgas 0.04 W/m×K 674.18 Calculated Property
λgas 0.05 W/m×K 755.63 Calculated Property
λgas 0.06 W/m×K 837.09 Calculated Property
λgas 0.07 W/m×K 918.54 Calculated Property
λgas 0.08 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.14; 0.09] W/m×K [266.90; 478.19] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A-4.67050e-02
Coefficient B-3.15720e+01
Coefficient C-1.23560e+00
Coefficient D-1.24630e-03
Coefficient E-2.61030e-07
Temperature range, min.266.90
Temperature range, max.478.19
λliquid 0.14 W/m×K 266.90 Calculated Property
λliquid 0.13 W/m×K 290.38 Calculated Property
λliquid 0.13 W/m×K 313.85 Calculated Property
λliquid 0.12 W/m×K 337.33 Calculated Property
λliquid 0.12 W/m×K 360.81 Calculated Property
λliquid 0.11 W/m×K 384.28 Calculated Property
λliquid 0.11 W/m×K 407.76 Calculated Property
λliquid 0.10 W/m×K 431.24 Calculated Property
λliquid 0.10 W/m×K 454.71 Calculated Property
λliquid 0.09 W/m×K 478.19 Calculated Property

Similar Compounds

Benzene, 1,2,3-trimethyl-. 1,2,4-Trimethylbenzene. Benzene, 1,2,3,5-tetramethyl-. Benzene, pentamethyl-. 1,2-Di(methyl-d3)benzene-d4. 2-Methylbenzyl radical. o-Xylene. Benzene, 1,2,4,5-tetramethyl-. 2,3,6-Trimethylbenzaldehyde. 1,2,4-Trimethyl-3-(chloromethyl)benzene. Benzonitrile, 3,4-dimethyl-. 2,3,4-Trimethylbenzaldehyde. 1,4-Dimethyl-2,3-bis(chloromethyl)benzene. 1,2,3-Trimethyl-4-(chloromethyl)benzene. 1,2-Dimethyl-3,6-bis(chloromethyl)benzene.

Find more compounds similar to Benzene, 1,2,3,4-tetramethyl-.

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