- InChI
- InChI=1S/C7H6N2O4/c1-5-6(8(10)11)3-2-4-7(5)9(12)13/h2-4H,1H3
- InChI Key
- XTRDKALNCIHHNI-UHFFFAOYSA-N
- Formula
- C7H6N2O4
- SMILES
-
Cc1c([N+](=O)[O-])cccc1[N+](=O
)[O-] - Molecular Weight1
- 182.13
- CAS
- 606-20-2
- Other Names
-
- 1-methyl-2,6-dinitrobenzene
- 2,6-DNT
- 2,6-DNT (2,6-dinitrotoluene)
- 2,6-dinitrotoluene
- 2-Methyl-1,3-dinitro-benzene
- 2-methyl-1,3-dinitrobenzene
- Rcra waste number U106
- toluene, 2,6-dinitro-
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- 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).
- ΔsubH : Enthalpy of sublimation 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.
- 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 | 0.7142 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | [-3574.00; -3556.80] | kJ/mol |
|
| ΔcH°solid | -3556.80 ± 1.00 | kJ/mol | NIST |
| ΔcH°solid | -3570.30 | kJ/mol | NIST |
| ΔcH°solid | -3560.90 ± 3.60 | kJ/mol | NIST |
| ΔcH°solid | -3574.00 | kJ/mol | NIST |
| μ | 2.81 | debye | ChemSep v8.3 pure component data Compiled value |
| EA | [1.47; 1.55] | eV |
|
| EA | 1.47 ± 0.05 | eV | NIST |
| EA | 1.55 ± 0.05 | eV | NIST |
| ΔfG° | 232.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | 28.60 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°solid | [-55.20; -41.80] | kJ/mol |
|
| ΔfH°solid | -55.20 ± 2.20 | kJ/mol | NIST |
| ΔfH°solid | -41.80 | kJ/mol | NIST |
| ΔfusH° | 29.87 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 76.83 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.87 | eV | Relay (1.0) Calculated Property |
| log10WS | [-3.00; -3.00] |
|
|
| log10WS | -3.00 | Aq. Solubility Prediction | |
| log10WS | -3.00 | Estimated Solubility | |
| logPoct/wat | 1.811 | Crippen Calculated Property | |
| McVol | 120.570 | ml/mol | McGowan Calculated Property |
| Pc | 3400.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 0.02 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [250.00; 1416.00] |
|
|
| Inp | 1416.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1401.00 | NIST | |
| Inp | 1415.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 250.87 | NIST | |
| Inp | 250.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Ip | [2322.00; 2322.00] |
|
|
| Ip | 2322.00 | NIST | |
| Ip | 2322.00 | NIST | |
| Tboil | 553.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 780.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [327.00; 339.19] | K |
|
| Tfus | 338.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 339.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 337.65 | K | Aq. Solubility Prediction |
| Tfus | 329.60 ± 0.20 | K | NIST |
| Tfus | 339.00 ± 3.00 | K | NIST |
| Tfus | 339.19 ± 0.10 | K | NIST |
| Tfus | 327.00 ± 0.10 | K | NIST |
| Ttriple | 337.85 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 4.38 | ChemSep v8.3 pure component data Compiled value | |
| URi | 5.70 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.487 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2420000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.24 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | [217.00; 224.00] | J/mol×K | [305.00; 305.00] |
|
| Cp,solid | 217.00 | J/mol×K | 305.00 | NIST |
| Cp,solid | 224.00 | J/mol×K | 305.00 | NIST |
| ΔfusH | [16.07; 23.85] | kJ/mol | [327.50; 340.00] |
|
| ΔfusH | 23.85 | kJ/mol | 327.50 | NIST |
| ΔfusH | 23.85 | kJ/mol | 327.50 | NIST |
| ΔfusH | 19.28 | kJ/mol | 340.00 | NIST |
| ΔfusH | 16.07 | kJ/mol | 340.00 | NIST |
| ΔsubH | [98.30; 99.60] | kJ/mol | [300.00; 300.00] |
|
| ΔsubH | 99.60 ± 2.30 | kJ/mol | 300.00 | NIST |
| ΔsubH | 98.30 ± 0.80 | kJ/mol | 300.00 | NIST |
| ΔvapH | [56.90; 77.80] | kJ/mol | [385.50; 488.00] |
|
| ΔvapH | 68.70 | kJ/mol | 385.50 | NIST |
| ΔvapH | 77.80 | kJ/mol | 431.50 | NIST |
| ΔvapH | 56.90 | kJ/mol | 488.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [158.57; 392.18] | J/mol×K | [273.00; 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 | 9.45120e+01 | |||
| Coefficient B | -5.82560e+02 | |||
| Coefficient C | 6.36224e+00 | |||
| Coefficient D | -2.65870e-04 | |||
| Coefficient E | 5.37350e-08 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 158.57 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 220.88 | J/mol×K | 409.33 | Calculated Property |
| Cp,gas | 269.65 | J/mol×K | 545.67 | Calculated Property |
| Cp,gas | 305.48 | J/mol×K | 682.00 | Calculated Property |
| Cp,gas | 331.68 | J/mol×K | 818.33 | Calculated Property |
| Cp,gas | 351.02 | J/mol×K | 954.67 | Calculated Property |
| Cp,gas | 365.53 | J/mol×K | 1091.00 | Calculated Property |
| Cp,gas | 376.60 | J/mol×K | 1227.33 | Calculated Property |
| Cp,gas | 385.25 | J/mol×K | 1363.67 | Calculated Property |
| Cp,gas | 392.18 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [263.63; 409.13] | J/mol×K | [337.85; 558.00] |
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 | 1.63490e+02 | |||
| Coefficient B | 7.85690e+02 | |||
| Coefficient C | -1.83936e+00 | |||
| Coefficient D | 1.45890e-02 | |||
| Coefficient E | -7.08330e-06 | |||
| Temperature range, min. | 337.85 | |||
| Temperature range, max. | 558.00 | |||
| Cp,liquid | 263.63 | J/mol×K | 337.85 | Calculated Property |
| Cp,liquid | 271.81 | J/mol×K | 362.31 | Calculated Property |
| Cp,liquid | 282.01 | J/mol×K | 386.77 | Calculated Property |
| Cp,liquid | 294.18 | J/mol×K | 411.23 | Calculated Property |
| Cp,liquid | 308.34 | J/mol×K | 435.69 | Calculated Property |
| Cp,liquid | 324.50 | J/mol×K | 460.16 | Calculated Property |
| Cp,liquid | 342.68 | J/mol×K | 484.62 | Calculated Property |
| Cp,liquid | 362.87 | J/mol×K | 509.08 | Calculated Property |
| Cp,liquid | 385.05 | J/mol×K | 533.54 | Calculated Property |
| Cp,liquid | 409.13 | J/mol×K | 558.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0046757; 0.0000304] | Pa×s | [337.85; 714.00] |
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 | -7.03860e+01 | |||
| Coefficient B | 5.31090e+03 | |||
| Coefficient C | 8.62620e+00 | |||
| Coefficient D | -8.11260e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 337.85 | |||
| Temperature range, max. | 714.00 | |||
| η | 0.0046757 | Pa×s | 337.85 | Calculated Property |
| η | 0.0017765 | Pa×s | 379.64 | Calculated Property |
| η | 0.0008325 | Pa×s | 421.44 | Calculated Property |
| η | 0.0004473 | Pa×s | 463.23 | Calculated Property |
| η | 0.0002627 | Pa×s | 505.03 | Calculated Property |
| η | 0.0001635 | Pa×s | 546.82 | Calculated Property |
| η | 0.0001054 | Pa×s | 588.62 | Calculated Property |
| η | 0.0000692 | Pa×s | 630.41 | Calculated Property |
| η | 0.0000459 | Pa×s | 672.21 | Calculated Property |
| η | 0.0000304 | Pa×s | 714.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [63.09; 21.32] | kJ/mol | [337.85; 770.00] |
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 | 1.04171e+02 | |||
| Coefficient B | 1.24753e+00 | |||
| Coefficient C | 3.09575e-02 | |||
| Coefficient D | -2.85186e+00 | |||
| Coefficient E | 1.93885e+00 | |||
| Critical temperature, Tc (K) | 7.80000e+02 | |||
| Temperature range, min. | 337.85 | |||
| Temperature range, max. | 770.00 | |||
| ΔvapH | 63.09 | kJ/mol | 337.85 | Calculated Property |
| ΔvapH | 60.35 | kJ/mol | 385.87 | Calculated Property |
| ΔvapH | 58.22 | kJ/mol | 433.88 | Calculated Property |
| ΔvapH | 56.54 | kJ/mol | 481.90 | Calculated Property |
| ΔvapH | 55.08 | kJ/mol | 529.92 | Calculated Property |
| ΔvapH | 53.49 | kJ/mol | 577.93 | Calculated Property |
| ΔvapH | 51.21 | kJ/mol | 625.95 | Calculated Property |
| ΔvapH | 47.28 | kJ/mol | 673.97 | Calculated Property |
| ΔvapH | 39.79 | kJ/mol | 721.98 | Calculated Property |
| ΔvapH | 21.32 | kJ/mol | 770.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [429.77; 611.84] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46496e+01 | |||
| Coefficient B | -4.86051e+03 | |||
| Coefficient C | -9.13380e+01 | |||
| Temperature range, min. | 429.77 | |||
| Temperature range, max. | 611.84 | |||
| Pvap | 1.33 | kPa | 429.77 | Calculated Property |
| Pvap | 3.00 | kPa | 450.00 | Calculated Property |
| Pvap | 6.18 | kPa | 470.23 | Calculated Property |
| Pvap | 11.84 | kPa | 490.46 | Calculated Property |
| Pvap | 21.31 | kPa | 510.69 | Calculated Property |
| Pvap | 36.32 | kPa | 530.92 | Calculated Property |
| Pvap | 59.08 | kPa | 551.15 | Calculated Property |
| Pvap | 92.24 | kPa | 571.38 | Calculated Property |
| Pvap | 138.91 | kPa | 591.61 | Calculated Property |
| Pvap | 202.65 | kPa | 611.84 | Calculated Property |
| Pvap | [0.02; 2152.30] | kPa | [337.85; 770.00] |
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 | 1.08858e+02 | |||
| Coefficient B | -1.20822e+04 | |||
| Coefficient C | -1.33178e+01 | |||
| Coefficient D | 5.09858e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 337.85 | |||
| Temperature range, max. | 770.00 | |||
| Pvap | 0.02 | kPa | 337.85 | Calculated Property |
| Pvap | 0.36 | kPa | 385.87 | Calculated Property |
| Pvap | 2.99 | kPa | 433.88 | Calculated Property |
| Pvap | 14.82 | kPa | 481.90 | Calculated Property |
| Pvap | 51.96 | kPa | 529.92 | Calculated Property |
| Pvap | 142.72 | kPa | 577.93 | Calculated Property |
| Pvap | 329.12 | kPa | 625.95 | Calculated Property |
| Pvap | 668.82 | kPa | 673.97 | Calculated Property |
| Pvap | 1240.14 | kPa | 721.98 | Calculated Property |
| Pvap | 2152.30 | kPa | 770.00 | Calculated Property |
| Pvap | [3.58e-03; 3634.97] | kPa | [339.00; 770.00] |
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 | 2.82485e+02 | |||
| Coefficient B | -2.25355e+04 | |||
| Coefficient C | -3.83779e+01 | |||
| Coefficient D | 1.69581e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 339.00 | |||
| Temperature range, max. | 770.00 | |||
| Pvap | 3.58e-03 | kPa | 339.00 | Calculated Property |
| Pvap | 0.15 | kPa | 386.89 | Calculated Property |
| Pvap | 2.05 | kPa | 434.78 | Calculated Property |
| Pvap | 13.42 | kPa | 482.67 | Calculated Property |
| Pvap | 54.79 | kPa | 530.56 | Calculated Property |
| Pvap | 164.69 | kPa | 578.44 | Calculated Property |
| Pvap | 406.93 | kPa | 626.33 | Calculated Property |
| Pvap | 891.45 | kPa | 674.22 | Calculated Property |
| Pvap | 1826.20 | kPa | 722.11 | Calculated Property |
| Pvap | 3634.97 | kPa | 770.00 | Calculated Property |
| Pvap | [1.65; 51.68] | kPa | [423.00; 533.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.75940e+00 | |||
| Coefficient B | -1.27012e+03 | |||
| Coefficient C | -2.69179e+02 | |||
| Reference | Maksimov, 1968, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 423.00 | |||
| Temperature range, max. | 533.00 | |||
| Pvap | 1.65 | kPa | 423.00 | Calculated Property |
| Pvap | 3.03 | kPa | 435.22 | Calculated Property |
| Pvap | 5.13 | kPa | 447.44 | Calculated Property |
| Pvap | 8.10 | kPa | 459.67 | Calculated Property |
| Pvap | 12.11 | kPa | 471.89 | Calculated Property |
| Pvap | 17.29 | kPa | 484.11 | Calculated Property |
| Pvap | 23.76 | kPa | 496.33 | Calculated Property |
| Pvap | 31.61 | kPa | 508.56 | Calculated Property |
| Pvap | 40.90 | kPa | 520.78 | Calculated Property |
| Pvap | 51.68 | kPa | 533.00 | Calculated Property |
| Pvap | [1.65; 51.68] | kPa | [423.00; 533.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.75940e+00 | |||
| Coefficient B | -1.27012e+03 | |||
| Coefficient C | -2.69179e+02 | |||
| Reference | Maksimov, 1968 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 423.00 | |||
| Temperature range, max. | 533.00 | |||
| Pvap | 1.65 | kPa | 423.00 | Calculated Property |
| Pvap | 3.03 | kPa | 435.22 | Calculated Property |
| Pvap | 5.13 | kPa | 447.44 | Calculated Property |
| Pvap | 8.10 | kPa | 459.67 | Calculated Property |
| Pvap | 12.11 | kPa | 471.89 | Calculated Property |
| Pvap | 17.29 | kPa | 484.11 | Calculated Property |
| Pvap | 23.76 | kPa | 496.33 | Calculated Property |
| Pvap | 31.61 | kPa | 508.56 | Calculated Property |
| Pvap | 40.90 | kPa | 520.78 | Calculated Property |
| Pvap | 51.68 | kPa | 533.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1332.40; 675.17] | kg/m3 | [337.85; 747.26] |
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 | 4.97807e+01 | |||
| Coefficient B | 1.74150e-01 | |||
| Coefficient C | 7.80000e+02 | |||
| Coefficient D | 2.23860e-01 | |||
| Temperature range, min. | 337.85 | |||
| Temperature range, max. | 747.26 | |||
| ρl | 1332.40 | kg/m3 | 337.85 | Calculated Property |
| ρl | 1284.05 | kg/m3 | 383.34 | Calculated Property |
| ρl | 1233.19 | kg/m3 | 428.83 | Calculated Property |
| ρl | 1179.28 | kg/m3 | 474.32 | Calculated Property |
| ρl | 1121.53 | kg/m3 | 519.81 | Calculated Property |
| ρl | 1058.80 | kg/m3 | 565.30 | Calculated Property |
| ρl | 989.23 | kg/m3 | 610.79 | Calculated Property |
| ρl | 909.49 | kg/m3 | 656.28 | Calculated Property |
| ρl | 812.42 | kg/m3 | 701.77 | Calculated Property |
| ρl | 675.17 | kg/m3 | 747.26 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.05; 2.94e-04] | N/m | [337.85; 770.00] |
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 | -1.28030e-02 | |||
| Coefficient B | 2.55040e+02 | |||
| Coefficient C | -4.01210e+00 | |||
| Coefficient D | 3.41590e-03 | |||
| Coefficient E | -5.54010e-06 | |||
| Temperature range, min. | 337.85 | |||
| Temperature range, max. | 770.00 | |||
| γ | 0.05 | N/m | 337.85 | Calculated Property |
| γ | 0.04 | N/m | 385.87 | Calculated Property |
| γ | 0.04 | N/m | 433.88 | Calculated Property |
| γ | 0.03 | N/m | 481.90 | Calculated Property |
| γ | 0.02 | N/m | 529.92 | Calculated Property |
| γ | 0.02 | N/m | 577.93 | Calculated Property |
| γ | 0.01 | N/m | 625.95 | Calculated Property |
| γ | 0.01 | N/m | 673.97 | Calculated Property |
| γ | 0.00 | N/m | 721.98 | Calculated Property |
| γ | 2.94e-04 | N/m | 770.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.05] | W/m×K | [274.00; 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 | 1.59320e-04 | |||
| Coefficient B | 9.23550e-01 | |||
| Coefficient C | 6.90150e+02 | |||
| Coefficient D | 1.97200e+04 | |||
| Temperature range, min. | 274.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 274.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 354.67 | Calculated Property |
| λgas | 0.02 | W/m×K | 435.33 | Calculated Property |
| λgas | 0.02 | W/m×K | 516.00 | Calculated Property |
| λgas | 0.03 | W/m×K | 596.67 | Calculated Property |
| λgas | 0.03 | W/m×K | 677.33 | Calculated Property |
| λgas | 0.04 | W/m×K | 758.00 | Calculated Property |
| λgas | 0.04 | W/m×K | 838.67 | Calculated Property |
| λgas | 0.05 | W/m×K | 919.33 | 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 | [337.85; 558.00] |
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 | -3.99010e-02 | |||
| Coefficient B | -9.94660e+01 | |||
| Coefficient C | -7.66810e-01 | |||
| Coefficient D | -1.93290e-03 | |||
| Coefficient E | 1.85120e-07 | |||
| Temperature range, min. | 337.85 | |||
| Temperature range, max. | 558.00 | |||
| λliquid | 0.14 | W/m×K | 337.85 | Calculated Property |
| λliquid | 0.14 | W/m×K | 362.31 | Calculated Property |
| λliquid | 0.13 | W/m×K | 386.77 | Calculated Property |
| λliquid | 0.13 | W/m×K | 411.23 | Calculated Property |
| λliquid | 0.13 | W/m×K | 435.69 | Calculated Property |
| λliquid | 0.12 | W/m×K | 460.16 | Calculated Property |
| λliquid | 0.11 | W/m×K | 484.62 | Calculated Property |
| λliquid | 0.11 | W/m×K | 509.08 | Calculated Property |
| λliquid | 0.10 | W/m×K | 533.54 | Calculated Property |
| λliquid | 0.10 | W/m×K | 558.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 2-methyl-1,3-dinitro-.
Mixtures
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
- Solubility of 4-Nitrotoluene, 2,6-Dinitrotoluene, 2,3-Dinitrotoluene, and 1,3,5-Trinitrobenzene in Pure Water and Seawater
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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