- InChI
- InChI=1S/C7H6N2O4/c1-5-2-3-6(8(10)11)4-7(5)9(12)13/h2-4H,1H3
- InChI Key
- RMBFBMJGBANMMK-UHFFFAOYSA-N
- Formula
- C7H6N2O4
- SMILES
-
Cc1ccc([N+](=O)[O-])cc1[N+](=O
)[O-] - Molecular Weight1
- 182.14
- CAS
- 121-14-2
- Other Names
-
- 1-methyl-2,4-dinitrobenzene
- 2,4-DNT
- 2,4-Dinitrotoluol
- 2,4-dinitrotoluene
- 4-Methyl-1,3-dinitrobenzene
- 6-Methyl-1,3-dinitrobenzene
- Dinitrotoluol
- NCI-C01865
- NSC 7194
- Rcra waste number U105
- Toluene, 2,4-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 standard conditions (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).
- Psub : Sublimation 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.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- 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 | 0.7126 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | [-3586.00; -3540.20] | kJ/mol |
|
| ΔcH°solid | -3545.60 ± 3.00 | kJ/mol | NIST |
| ΔcH°solid | -3572.00 | kJ/mol | NIST |
| ΔcH°solid | -3540.20 ± 3.60 | kJ/mol | NIST |
| ΔcH°solid | -3551.20 | kJ/mol | NIST |
| ΔcH°solid | -3586.00 | kJ/mol | NIST |
| ΔcH°solid | -3568.00 | kJ/mol | NIST |
| μ | 4.32 | debye | ChemSep v8.3 pure component data Compiled value |
| EA | 1.60 ± 0.05 | eV | NIST |
| ΔfG° | 218.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [33.20; 33.60] | kJ/mol |
|
| ΔfH°gas | 33.60 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | 33.20 ± 3.30 | kJ/mol | NIST |
| ΔfH°solid | [-66.40; -29.00] | kJ/mol |
|
| ΔfH°solid | -66.40 ± 3.00 | kJ/mol | NIST |
| ΔfH°solid | -40.00 | kJ/mol | NIST |
| ΔfH°solid | -29.00 | kJ/mol | NIST |
| ΔfusH° | 29.87 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [99.60; 100.00] | kJ/mol |
|
| ΔsubH° | 99.60 ± 2.50 | kJ/mol | NIST |
| ΔsubH° | 100.00 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 74.17 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.97 | eV | Relay (1.0) Calculated Property |
| log10WS | [-2.82; -2.82] |
|
|
| log10WS | -2.82 | Aq. Solubility Prediction | |
| log10WS | -2.82 | 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 | 7.87e-03 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [261.80; 1550.09] |
|
|
| Inp | 1497.00 | NIST | |
| Inp | 1549.11 | NIST | |
| Inp | 1550.09 | NIST | |
| Inp | 1497.00 | NIST | |
| Inp | 1537.00 | NIST | |
| Inp | 1531.81 | NIST | |
| Inp | 1541.10 | NIST | |
| Inp | 1498.00 | NIST | |
| Inp | 1537.00 | NIST | |
| Inp | Outlier 262.61 | NIST | |
| Inp | Outlier 261.80 | NIST | |
| Inp | 1549.11 | NIST | |
| Ip | [2420.00; 2420.00] |
|
|
| Ip | 2420.00 | NIST | |
| Ip | 2420.00 | NIST | |
| Ip | 2420.00 | NIST | |
| Tboil | 553.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 814.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [333.00; 345.00] | K |
|
| Tfus | 342.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | Outlier 333.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 342.53 | K | Aq. Solubility Prediction |
| Tfus | 341.00 ± 0.10 | K | NIST |
| Tfus | 344.30 ± 0.50 | K | NIST |
| Tfus | 345.00 ± 1.00 | K | NIST |
| Tfus | 343.00 ± 1.50 | K | NIST |
| Tfus | 340.00 ± 1.00 | K | NIST |
| Tfus | 345.00 ± 1.00 | K | NIST |
| Ttriple | 342.65 | 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 | 0.2450000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.24 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
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 | [264.32; 442.70] | J/mol×K | [342.65; 590.00] |
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 | 8.89580e+01 | |||
| Coefficient B | 1.32440e+03 | |||
| Coefficient C | -4.15496e+00 | |||
| Coefficient D | 1.97210e-02 | |||
| Coefficient E | -1.10790e-05 | |||
| Temperature range, min. | 342.65 | |||
| Temperature range, max. | 590.00 | |||
| Cp,liquid | 264.32 | J/mol×K | 342.65 | Calculated Property |
| Cp,liquid | 271.10 | J/mol×K | 370.13 | Calculated Property |
| Cp,liquid | 282.54 | J/mol×K | 397.62 | Calculated Property |
| Cp,liquid | 297.86 | J/mol×K | 425.10 | Calculated Property |
| Cp,liquid | 316.52 | J/mol×K | 452.58 | Calculated Property |
| Cp,liquid | 338.07 | J/mol×K | 480.07 | Calculated Property |
| Cp,liquid | 362.05 | J/mol×K | 507.55 | Calculated Property |
| Cp,liquid | 387.92 | J/mol×K | 535.03 | Calculated Property |
| Cp,liquid | 415.05 | J/mol×K | 562.52 | Calculated Property |
| Cp,liquid | 442.70 | J/mol×K | 590.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0034573; 0.0000481] | Pa×s | [342.65; 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 | -4.14080e+01 | |||
| Coefficient B | 3.94770e+03 | |||
| Coefficient C | 4.22030e+00 | |||
| Coefficient D | -3.51780e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 342.65 | |||
| Temperature range, max. | 714.00 | |||
| η | 0.0034573 | Pa×s | 342.65 | Calculated Property |
| η | 0.0014574 | Pa×s | 383.91 | Calculated Property |
| η | 0.0007350 | Pa×s | 425.17 | Calculated Property |
| η | 0.0004199 | Pa×s | 466.43 | Calculated Property |
| η | 0.0002620 | Pa×s | 507.69 | Calculated Property |
| η | 0.0001742 | Pa×s | 548.96 | Calculated Property |
| η | 0.0001213 | Pa×s | 590.22 | Calculated Property |
| η | 0.0000873 | Pa×s | 631.48 | Calculated Property |
| η | 0.0000643 | Pa×s | 672.74 | Calculated Property |
| η | 0.0000481 | Pa×s | 714.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [69.60; 31.72] | kJ/mol | [342.65; 789.19] |
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 | 1.29190e+02 | |||
| Coefficient B | 1.32480e+00 | |||
| Coefficient C | 1.08720e+00 | |||
| Coefficient D | -4.87370e+00 | |||
| Coefficient E | 2.85800e+00 | |||
| Critical temperature, Tc (K) | 8.14000e+02 | |||
| Temperature range, min. | 342.65 | |||
| Temperature range, max. | 789.19 | |||
| ΔvapH | 69.60 | kJ/mol | 342.65 | Calculated Property |
| ΔvapH | 65.34 | kJ/mol | 392.27 | Calculated Property |
| ΔvapH | 62.09 | kJ/mol | 441.88 | Calculated Property |
| ΔvapH | 59.71 | kJ/mol | 491.50 | Calculated Property |
| ΔvapH | 57.96 | kJ/mol | 541.11 | Calculated Property |
| ΔvapH | 56.50 | kJ/mol | 590.73 | Calculated Property |
| ΔvapH | 54.78 | kJ/mol | 640.34 | Calculated Property |
| ΔvapH | 51.85 | kJ/mol | 689.96 | Calculated Property |
| ΔvapH | 45.86 | kJ/mol | 739.57 | Calculated Property |
| ΔvapH | 31.72 | kJ/mol | 789.19 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [434.64; 630.47] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.78315e+01 | |||
| Coefficient B | -8.56181e+03 | |||
| Coefficient C | 5.33810e+01 | |||
| Temperature range, min. | 434.64 | |||
| Temperature range, max. | 630.47 | |||
| Pvap | 1.33 | kPa | 434.64 | Calculated Property |
| Pvap | 2.82 | kPa | 456.40 | Calculated Property |
| Pvap | 5.61 | kPa | 478.16 | Calculated Property |
| Pvap | 10.56 | kPa | 499.92 | Calculated Property |
| Pvap | 18.97 | kPa | 521.68 | Calculated Property |
| Pvap | 32.64 | kPa | 543.43 | Calculated Property |
| Pvap | 54.07 | kPa | 565.19 | Calculated Property |
| Pvap | 86.54 | kPa | 586.95 | Calculated Property |
| Pvap | 134.30 | kPa | 608.71 | Calculated Property |
| Pvap | 202.66 | kPa | 630.47 | Calculated Property |
| Pvap | [7.64e-03; 2199.17] | kPa | [342.65; 814.00] |
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 | 1.22025e+02 | |||
| Coefficient B | -1.33934e+04 | |||
| Coefficient C | -1.51574e+01 | |||
| Coefficient D | 5.59704e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 342.65 | |||
| Temperature range, max. | 814.00 | |||
| Pvap | 7.64e-03 | kPa | 342.65 | Calculated Property |
| Pvap | 0.20 | kPa | 395.02 | Calculated Property |
| Pvap | 2.01 | kPa | 447.39 | Calculated Property |
| Pvap | 11.40 | kPa | 499.77 | Calculated Property |
| Pvap | 43.53 | kPa | 552.14 | Calculated Property |
| Pvap | 126.54 | kPa | 604.51 | Calculated Property |
| Pvap | 304.11 | kPa | 656.88 | Calculated Property |
| Pvap | 639.52 | kPa | 709.26 | Calculated Property |
| Pvap | 1224.82 | kPa | 761.63 | Calculated Property |
| Pvap | 2199.17 | kPa | 814.00 | Calculated Property |
| Pvap | [0.02; 3409.11] | kPa | [343.00; 814.00] |
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 | 1.43080e+01 | |||
| Coefficient B | -6.62964e+03 | |||
| Coefficient C | 1.74908e-01 | |||
| Coefficient D | 1.20512e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 343.00 | |||
| Temperature range, max. | 814.00 | |||
| Pvap | 0.02 | kPa | 343.00 | Calculated Property |
| Pvap | 0.29 | kPa | 395.33 | Calculated Property |
| Pvap | 2.24 | kPa | 447.67 | Calculated Property |
| Pvap | 11.44 | kPa | 500.00 | Calculated Property |
| Pvap | 43.69 | kPa | 552.33 | Calculated Property |
| Pvap | 134.92 | kPa | 604.67 | Calculated Property |
| Pvap | 355.01 | kPa | 657.00 | Calculated Property |
| Pvap | 825.68 | kPa | 709.33 | Calculated Property |
| Pvap | 1743.43 | kPa | 761.67 | Calculated Property |
| Pvap | 3409.11 | kPa | 814.00 | Calculated Property |
| Pvap | [5.06; 65.77] | kPa | [473.00; 572.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.30438e+01 | |||
| Coefficient B | -3.90445e+03 | |||
| Coefficient C | -1.31199e+02 | |||
| Reference | Maksimov, 1968, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 473.00 | |||
| Temperature range, max. | 572.00 | |||
| Pvap | 5.06 | kPa | 473.00 | Calculated Property |
| Pvap | 7.22 | kPa | 484.00 | Calculated Property |
| Pvap | 10.09 | kPa | 495.00 | Calculated Property |
| Pvap | 13.82 | kPa | 506.00 | Calculated Property |
| Pvap | 18.61 | kPa | 517.00 | Calculated Property |
| Pvap | 24.63 | kPa | 528.00 | Calculated Property |
| Pvap | 32.12 | kPa | 539.00 | Calculated Property |
| Pvap | 41.30 | kPa | 550.00 | Calculated Property |
| Pvap | 52.43 | kPa | 561.00 | Calculated Property |
| Pvap | 65.77 | kPa | 572.00 | Calculated Property |
| Pvap | [5.06; 65.77] | kPa | [473.00; 572.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.30438e+01 | |||
| Coefficient B | -3.90445e+03 | |||
| Coefficient C | -1.31199e+02 | |||
| Reference | Maksimov, 1968 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 473.00 | |||
| Temperature range, max. | 572.00 | |||
| Pvap | 5.06 | kPa | 473.00 | Calculated Property |
| Pvap | 7.22 | kPa | 484.00 | Calculated Property |
| Pvap | 10.09 | kPa | 495.00 | Calculated Property |
| Pvap | 13.82 | kPa | 506.00 | Calculated Property |
| Pvap | 18.61 | kPa | 517.00 | Calculated Property |
| Pvap | 24.63 | kPa | 528.00 | Calculated Property |
| Pvap | 32.12 | kPa | 539.00 | Calculated Property |
| Pvap | 41.30 | kPa | 550.00 | Calculated Property |
| Pvap | 52.43 | kPa | 561.00 | Calculated Property |
| Pvap | 65.77 | kPa | 572.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1388.73; 677.08] | kg/m3 | [273.15; 789.19] |
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 | 9.30338e+01 | |||
| Coefficient B | 2.40370e-01 | |||
| Coefficient C | 8.14000e+02 | |||
| Coefficient D | 2.68060e-01 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 789.19 | |||
| ρl | 1388.73 | kg/m3 | 273.15 | Calculated Property |
| ρl | 1337.20 | kg/m3 | 330.49 | Calculated Property |
| ρl | 1283.17 | kg/m3 | 387.83 | Calculated Property |
| ρl | 1226.05 | kg/m3 | 445.16 | Calculated Property |
| ρl | 1165.02 | kg/m3 | 502.50 | Calculated Property |
| ρl | 1098.84 | kg/m3 | 559.84 | Calculated Property |
| ρl | 1025.46 | kg/m3 | 617.18 | Calculated Property |
| ρl | 941.04 | kg/m3 | 674.51 | Calculated Property |
| ρl | 836.67 | kg/m3 | 731.85 | Calculated Property |
| ρl | 677.08 | kg/m3 | 789.19 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.05; 0.00] | N/m | [342.65; 789.19] |
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 | -7.63260e-02 | |||
| Coefficient B | -4.62990e+00 | |||
| Coefficient C | -1.64780e+00 | |||
| Coefficient D | -1.20280e-03 | |||
| Coefficient E | 7.99650e-08 | |||
| Temperature range, min. | 342.65 | |||
| Temperature range, max. | 789.19 | |||
| γ | 0.05 | N/m | 342.65 | Calculated Property |
| γ | 0.04 | N/m | 392.27 | Calculated Property |
| γ | 0.04 | N/m | 441.88 | Calculated Property |
| γ | 0.03 | N/m | 491.50 | Calculated Property |
| γ | 0.03 | N/m | 541.11 | Calculated Property |
| γ | 0.02 | N/m | 590.73 | Calculated Property |
| γ | 0.02 | N/m | 640.34 | Calculated Property |
| γ | 0.01 | N/m | 689.96 | Calculated Property |
| γ | 0.01 | N/m | 739.57 | Calculated Property |
| γ | 0.00 | N/m | 789.19 | 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 | 1.18520e-04 | |||
| Coefficient B | 9.59140e-01 | |||
| Coefficient C | 7.34050e+02 | |||
| Coefficient D | 1.38960e+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 | 0.01 | W/m×K | 435.33 | Calculated Property |
| λgas | 0.02 | W/m×K | 516.00 | Calculated Property |
| λgas | 0.02 | W/m×K | 596.67 | Calculated Property |
| λgas | 0.03 | W/m×K | 677.33 | Calculated Property |
| λgas | 0.03 | 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 | [0.15; 0.10] | W/m×K | [342.65; 590.00] |
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 | -5.70010e-02 | |||
| Coefficient B | -6.70100e+01 | |||
| Coefficient C | -9.01940e-01 | |||
| Coefficient D | -1.36140e-03 | |||
| Coefficient E | -3.02090e-08 | |||
| Temperature range, min. | 342.65 | |||
| Temperature range, max. | 590.00 | |||
| λliquid | 0.15 | W/m×K | 342.65 | Calculated Property |
| λliquid | 0.15 | W/m×K | 370.13 | Calculated Property |
| λliquid | 0.14 | W/m×K | 397.62 | Calculated Property |
| λliquid | 0.14 | W/m×K | 425.10 | Calculated Property |
| λliquid | 0.13 | W/m×K | 452.58 | Calculated Property |
| λliquid | 0.13 | W/m×K | 480.07 | Calculated Property |
| λliquid | 0.12 | W/m×K | 507.55 | Calculated Property |
| λliquid | 0.11 | W/m×K | 535.03 | Calculated Property |
| λliquid | 0.11 | W/m×K | 562.52 | Calculated Property |
| λliquid | 0.10 | W/m×K | 590.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1-methyl-2,4-dinitro-.
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
- Triacetone triperoxide thermogravimetric study of vapor pressure and enthalpy of sublimation in 303 338 K temperature range
- New method for determination of vaporization and sublimation enthalpy of aromatic compounds at 298.15 K using solution calorimetry technique and group-additivity scheme
- Enthalpies of fusion and enthalpies of solvation of aromatic hydrocarbons derivatives: Estimation of sublimation enthalpies at 298.15K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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