| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.8512 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | [-3029.60; -3020.00] | kJ/mol |
|
| ΔcH°solid | -3020.00 ± 1.30 | kJ/mol | NIST |
| ΔcH°solid | -3022.40 ± 0.50 | kJ/mol | NIST |
| ΔcH°solid | -3024.70 | kJ/mol | NIST |
| ΔcH°solid | -3024.70 | kJ/mol | NIST |
| ΔcH°solid | -3025.00 | kJ/mol | NIST |
| ΔcH°solid | -3023.60 | kJ/mol | NIST |
| ΔcH°solid | -3026.80 | kJ/mol | NIST |
| ΔcH°solid | -3026.80 | kJ/mol | NIST |
| ΔcH°solid | -3029.60 | kJ/mol | NIST |
| ΔcH°solid | -3029.00 ± 0.40 | kJ/mol | NIST |
| ΔcH°solid | -3027.29 | kJ/mol | NIST |
| ΔcH°solid | -3022.90 | kJ/mol | NIST |
| μ | 2.65 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -395.40 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-495.80; -489.00] | kJ/mol |
|
| ΔfH°gas | -494.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -495.80 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | -493.40 | kJ/mol | NIST |
| ΔfH°gas | -489.00 | kJ/mol | NIST |
| ΔfH°solid | [-592.10; -585.30] | kJ/mol |
|
| ΔfH°solid | -592.10 ± 1.30 | kJ/mol | NIST |
| ΔfH°solid | -589.70 ± 1.10 | kJ/mol | NIST |
| ΔfH°solid | -585.30 | kJ/mol | NIST |
| ΔfusH° | [24.06; 27.09] | kJ/mol |
|
| ΔfusH° | 24.06 | kJ/mol | Solubility of salicylic acid in pure alcohols at different temperatures |
| ΔfusH° | 27.09 | kJ/mol | Solubility and Melting Properties of Salicylic Acid |
| ΔsubH° | [81.75; 96.30] | kJ/mol |
|
| ΔsubH° | 94.40 ± 0.40 | kJ/mol | NIST |
| ΔsubH° | 96.27 ± 0.49 | kJ/mol | NIST |
| ΔsubH° | 96.30 | kJ/mol | NIST |
| ΔsubH° | 96.30 ± 0.50 | kJ/mol | NIST |
| ΔsubH° | 95.70 ± 0.10 | kJ/mol | NIST |
| ΔsubH° | 95.10 ± 0.40 | kJ/mol | NIST |
| ΔsubH° | Outlier 81.75 | kJ/mol | NIST |
| ΔvapH° | 80.11 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.59 | eV | Relay (1.0) Calculated Property |
| log10WS | [-1.93; -1.85] |
|
|
| log10WS | -1.85 | Aq. Solubility Prediction | |
| log10WS | -1.93 | Aq. Solubility Prediction | |
| logPoct/wat | 1.090 | Crippen Calculated Property | |
| McVol | 99.040 | ml/mol | McGowan Calculated Property |
| Pc | 5180.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 2.80 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1263.00; 1342.00] |
|
|
| Inp | 1277.00 | NIST | |
| Inp | 1266.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1330.00 | NIST | |
| Inp | 1295.80 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1330.00 | NIST | |
| Inp | 1330.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1342.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1277.00 | NIST | |
| Inp | 1295.80 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1294.00 | NIST | |
| S°solid,1 bar | [172.40; 178.20] | J/mol×K |
|
| S°solid,1 bar | 172.40 | J/mol×K | NIST |
| S°solid,1 bar | 178.20 | J/mol×K | NIST |
| Tboil | 529.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 739.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [430.00; 432.70] | K |
|
| Tfus | 432.15 | K | Liquid pharmaceuticals formulation by eutectic formation |
| Tfus | 432.70 | K | Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements |
| Tfus | 432.00 | K | Polar Mixed-Solid Solute Systems in Supercritical Carbon Dioxide: Entrainer Effect and Its Influence on Solubility and Selectivity |
| Tfus | 431.75 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 431.92 | K | Aq. Solubility Prediction |
| Tfus | 431.92 | K | Aq. Solubility Prediction |
| Tfus | 432.00 ± 1.50 | K | NIST |
| Tfus | 431.45 ± 0.50 | K | NIST |
| Tfus | Outlier 430.00 ± 4.00 | K | NIST |
| Tfus | 432.10 ± 0.80 | K | NIST |
| Tfus | 432.00 ± 0.80 | K | NIST |
| Tfus | 432.10 ± 0.80 | K | NIST |
| Tfus | 432.20 ± 0.80 | K | NIST |
| Ttriple | 431.75 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 3.62 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.69 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.364 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2750000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.28 | ChemSep v8.3 pure component data Compiled value |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 484.20 | K | 2.70 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [115.11; 282.14] | J/mol×K | [273.00; 1000.15] |
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 | 8.33880e+01 | |||
| Coefficient B | -8.79570e+02 | |||
| Coefficient C | 7.00924e+00 | |||
| Coefficient D | -1.34990e-03 | |||
| Coefficient E | 5.12200e-07 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.15 | |||
| Cp,gas | 115.11 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 144.31 | J/mol×K | 353.79 | Calculated Property |
| Cp,gas | 172.99 | J/mol×K | 434.59 | Calculated Property |
| Cp,gas | 198.16 | J/mol×K | 515.38 | Calculated Property |
| Cp,gas | 219.19 | J/mol×K | 596.18 | Calculated Property |
| Cp,gas | 236.45 | J/mol×K | 676.97 | Calculated Property |
| Cp,gas | 250.67 | J/mol×K | 757.77 | Calculated Property |
| Cp,gas | 262.59 | J/mol×K | 838.56 | Calculated Property |
| Cp,gas | 272.89 | J/mol×K | 919.36 | Calculated Property |
| Cp,gas | 282.14 | J/mol×K | 1000.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [265.87; 324.09] | J/mol×K | [431.75; 551.75] |
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 | 1.29500e+02 | |||
| Coefficient B | 1.60820e+02 | |||
| Coefficient C | 1.60274e+00 | |||
| Coefficient D | 9.29210e-03 | |||
| Coefficient E | -5.74930e-06 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 431.75 | |||
| Temperature range, max. | 551.75 | |||
| Cp,liquid | 265.87 | J/mol×K | 431.75 | Calculated Property |
| Cp,liquid | 272.22 | J/mol×K | 445.08 | Calculated Property |
| Cp,liquid | 278.66 | J/mol×K | 458.42 | Calculated Property |
| Cp,liquid | 285.16 | J/mol×K | 471.75 | Calculated Property |
| Cp,liquid | 291.71 | J/mol×K | 485.08 | Calculated Property |
| Cp,liquid | 298.27 | J/mol×K | 498.42 | Calculated Property |
| Cp,liquid | 304.81 | J/mol×K | 511.75 | Calculated Property |
| Cp,liquid | 311.32 | J/mol×K | 525.08 | Calculated Property |
| Cp,liquid | 317.75 | J/mol×K | 538.42 | Calculated Property |
| Cp,liquid | 324.09 | J/mol×K | 551.75 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0014490; 0.0002120] | Pa×s | [426.15; 639.00] |
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 | -5.07430e+01 | |||
| Coefficient B | 5.20360e+03 | |||
| Coefficient C | 5.28370e+00 | |||
| Coefficient D | 2.04700e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 426.15 | |||
| Temperature range, max. | 639.00 | |||
| η | 0.0014490 | Pa×s | 426.15 | Calculated Property |
| η | 0.0010148 | Pa×s | 449.80 | Calculated Property |
| η | 0.0007468 | Pa×s | 473.45 | Calculated Property |
| η | 0.0005730 | Pa×s | 497.10 | Calculated Property |
| η | 0.0004556 | Pa×s | 520.75 | Calculated Property |
| η | 0.0003734 | Pa×s | 544.40 | Calculated Property |
| η | 0.0003142 | Pa×s | 568.05 | Calculated Property |
| η | 0.0002704 | Pa×s | 591.70 | Calculated Property |
| η | 0.0002373 | Pa×s | 615.35 | Calculated Property |
| η | 0.0002120 | Pa×s | 639.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [75.28; 22.79] | kJ/mol | [431.75; 722.83] |
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 | 1.33250e+02 | |||
| Coefficient B | -1.18490e-01 | |||
| Coefficient C | 3.60620e+00 | |||
| Coefficient D | -5.16350e+00 | |||
| Coefficient E | 2.13000e+00 | |||
| Critical temperature, Tc (K) | 7.39000e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 431.75 | |||
| Temperature range, max. | 722.83 | |||
| ΔvapH | 75.28 | kJ/mol | 431.75 | Calculated Property |
| ΔvapH | 70.95 | kJ/mol | 464.09 | Calculated Property |
| ΔvapH | 66.82 | kJ/mol | 496.43 | Calculated Property |
| ΔvapH | 62.79 | kJ/mol | 528.78 | Calculated Property |
| ΔvapH | 58.74 | kJ/mol | 561.12 | Calculated Property |
| ΔvapH | 54.46 | kJ/mol | 593.46 | Calculated Property |
| ΔvapH | 49.67 | kJ/mol | 625.80 | Calculated Property |
| ΔvapH | 43.85 | kJ/mol | 658.15 | Calculated Property |
| ΔvapH | 35.99 | kJ/mol | 690.49 | Calculated Property |
| ΔvapH | 22.79 | kJ/mol | 722.83 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.58; 5224.56] | kPa | [429.95; 739.00] |
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 | 2.45634e+02 | |||
| Coefficient B | -2.11489e+04 | |||
| Coefficient C | -3.26392e+01 | |||
| Coefficient D | 1.30693e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 429.95 | |||
| Temperature range, max. | 739.00 | |||
| Pvap | 2.58 | kPa | 429.95 | Calculated Property |
| Pvap | 11.92 | kPa | 464.29 | Calculated Property |
| Pvap | 41.21 | kPa | 498.63 | Calculated Property |
| Pvap | 114.51 | kPa | 532.97 | Calculated Property |
| Pvap | 269.99 | kPa | 567.31 | Calculated Property |
| Pvap | 562.60 | kPa | 601.64 | Calculated Property |
| Pvap | 1068.81 | kPa | 635.98 | Calculated Property |
| Pvap | 1896.36 | kPa | 670.32 | Calculated Property |
| Pvap | 3202.35 | kPa | 704.66 | Calculated Property |
| Pvap | 5224.56 | kPa | 739.00 | Calculated Property |
| Pvap | [2.71; 6185.51] | kPa | [431.75; 739.00] |
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 | 4.74158e+02 | |||
| Coefficient B | -3.34417e+04 | |||
| Coefficient C | -6.61599e+01 | |||
| Coefficient D | 3.08189e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 431.75 | |||
| Temperature range, max. | 739.00 | |||
| Pvap | 2.71 | kPa | 431.75 | Calculated Property |
| Pvap | 13.24 | kPa | 465.89 | Calculated Property |
| Pvap | 45.69 | kPa | 500.03 | Calculated Property |
| Pvap | 123.34 | kPa | 534.17 | Calculated Property |
| Pvap | 280.60 | kPa | 568.31 | Calculated Property |
| Pvap | 568.93 | kPa | 602.44 | Calculated Property |
| Pvap | 1072.29 | kPa | 636.58 | Calculated Property |
| Pvap | 1940.48 | kPa | 670.72 | Calculated Property |
| Pvap | 3457.41 | kPa | 704.86 | Calculated Property |
| Pvap | 6185.51 | kPa | 739.00 | Calculated Property |
| Pvap | [0.13; 103.43] | kPa | [386.80; 529.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.28341e+01 | |||
| Coefficient B | -2.59274e+03 | |||
| Coefficient C | -2.12625e+02 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 386.80 | |||
| Temperature range, max. | 529.00 | |||
| Pvap | 0.13 | kPa | 386.80 | Calculated Property |
| Pvap | 0.44 | kPa | 402.60 | Calculated Property |
| Pvap | 1.26 | kPa | 418.40 | Calculated Property |
| Pvap | 3.10 | kPa | 434.20 | Calculated Property |
| Pvap | 6.76 | kPa | 450.00 | Calculated Property |
| Pvap | 13.37 | kPa | 465.80 | Calculated Property |
| Pvap | 24.40 | kPa | 481.60 | Calculated Property |
| Pvap | 41.66 | kPa | 497.40 | Calculated Property |
| Pvap | 67.23 | kPa | 513.20 | Calculated Property |
| Pvap | 103.43 | kPa | 529.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1160.93; 653.86] | kg/m3 | [426.15; 722.53] |
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 | 1.16463e+02 | |||
| Coefficient B | 2.75220e-01 | |||
| Coefficient C | 7.39000e+02 | |||
| Coefficient D | 2.85740e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 426.15 | |||
| Temperature range, max. | 722.53 | |||
| ρl | 1160.93 | kg/m3 | 426.15 | Calculated Property |
| ρl | 1124.85 | kg/m3 | 459.08 | Calculated Property |
| ρl | 1086.87 | kg/m3 | 492.01 | Calculated Property |
| ρl | 1046.56 | kg/m3 | 524.94 | Calculated Property |
| ρl | 1003.31 | kg/m3 | 557.87 | Calculated Property |
| ρl | 956.18 | kg/m3 | 590.81 | Calculated Property |
| ρl | 903.67 | kg/m3 | 623.74 | Calculated Property |
| ρl | 842.96 | kg/m3 | 656.67 | Calculated Property |
| ρl | 767.65 | kg/m3 | 689.60 | Calculated Property |
| ρl | 653.86 | kg/m3 | 722.53 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [431.75; 722.83] |
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 | -2.53990e-02 | |||
| Coefficient B | 3.55610e+01 | |||
| Coefficient C | -2.63500e+00 | |||
| Coefficient D | 2.69140e-04 | |||
| Coefficient E | -2.37830e-06 | |||
| Comment | ChemSep eq 16, SurfaceTension | |||
| Temperature range, min. | 431.75 | |||
| Temperature range, max. | 722.83 | |||
| γ | 0.03 | N/m | 431.75 | Calculated Property |
| γ | 0.03 | N/m | 464.09 | Calculated Property |
| γ | 0.02 | N/m | 496.43 | Calculated Property |
| γ | 0.02 | N/m | 528.78 | Calculated Property |
| γ | 0.02 | N/m | 561.12 | Calculated Property |
| γ | 0.01 | N/m | 593.46 | Calculated Property |
| γ | 0.01 | N/m | 625.80 | Calculated Property |
| γ | 0.01 | N/m | 658.15 | Calculated Property |
| γ | 0.00 | N/m | 690.49 | Calculated Property |
| γ | 0.00 | N/m | 722.83 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [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 λ in W/m×K, T in K | |||
| Coefficient A | 2.83370e-05 | |||
| Coefficient B | 1.10430e+00 | |||
| Coefficient C | 1.06430e+02 | |||
| Coefficient D | 6.77830e+04 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 274.00 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.01 | W/m×K | 274.00 | Calculated Property |
| λ | 0.01 | W/m×K | 354.67 | Calculated Property |
| λ | 0.01 | W/m×K | 435.33 | Calculated Property |
| λ | 0.02 | W/m×K | 516.00 | Calculated Property |
| λ | 0.02 | W/m×K | 596.67 | Calculated Property |
| λ | 0.03 | W/m×K | 677.33 | Calculated Property |
| λ | 0.03 | W/m×K | 758.00 | Calculated Property |
| λ | 0.04 | W/m×K | 838.67 | Calculated Property |
| λ | 0.04 | W/m×K | 919.33 | Calculated Property |
| λ | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.12; 0.10] | W/m×K | [431.75; 529.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 4.37990e-03 | |||
| Coefficient B | -3.91310e+02 | |||
| Coefficient C | 6.35440e-01 | |||
| Coefficient D | -4.83230e-03 | |||
| Coefficient E | 1.09950e-06 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 431.75 | |||
| Temperature range, max. | 529.00 | |||
| λ | 0.12 | W/m×K | 431.75 | Calculated Property |
| λ | 0.12 | W/m×K | 442.56 | Calculated Property |
| λ | 0.12 | W/m×K | 453.36 | Calculated Property |
| λ | 0.11 | W/m×K | 464.17 | Calculated Property |
| λ | 0.11 | W/m×K | 474.97 | Calculated Property |
| λ | 0.11 | W/m×K | 485.78 | Calculated Property |
| λ | 0.11 | W/m×K | 496.58 | Calculated Property |
| λ | 0.10 | W/m×K | 507.39 | Calculated Property |
| λ | 0.10 | W/m×K | 518.19 | Calculated Property |
| λ | 0.10 | W/m×K | 529.00 | Calculated Property |
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