- InChI
- InChI=1S/C3H4O2/c1-2-3(4)5/h2H,1H2,(H,4,5)
- InChI Key
- NIXOWILDQLNWCW-UHFFFAOYSA-N
- Formula
- C3H4O2
- SMILES
- C=CC(=O)O
- Molecular Weight1
- 72.06
- CAS
- 79-10-7
- Other Names
-
- Acroleic acid
- CH2=CHCOOH
- Ethylenecarboxylic acid
- Glacial acrylic acid
- Kyselina akrylova
- NSC 4765
- Propene acid
- Rcra waste number U008
- acrylic acid
- propenoic acid
- vinylformic acid
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- 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 | [0.2207; 0.5600] |
|
|
| ω | 0.5600 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2207 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.5600 | KDB | |
| Tig | 463.15 | K | KDB |
| ΔcH°liquid | [-1374.00; -1368.80] | kJ/mol |
|
| ΔcH°liquid | -1368.80 ± 1.80 | kJ/mol | NIST |
| ΔcH°liquid | -1374.00 ± 11.00 | kJ/mol | NIST |
| ΔcH°liquid | -1373.00 ± 5.00 | kJ/mol | NIST |
| μ | 1.46 | debye | ChemSep v8.3 pure component data Compiled value |
| LFL | 2.40 | % in Air | KDB |
| Tflash,cc | 320.93 | K | KDB |
| ΔfG° | [-286.30; -286.10] | kJ/mol |
|
| ΔfG° | -286.10 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -286.30 | kJ/mol | KDB |
| ΔfH°gas | [-337.10; -324.70] | kJ/mol |
|
| ΔfH°gas | -337.10 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -336.50 | kJ/mol | KDB |
| ΔfH°gas | -330.70 ± 4.20 | kJ/mol | NIST |
| ΔfH°gas | -324.70 | kJ/mol | NIST |
| ΔfH°gas | -336.90 ± 2.30 | kJ/mol | NIST |
| ΔfH°liquid | [-383.80; -377.80] | kJ/mol |
|
| ΔfH°liquid | -383.80 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -377.80 ± 9.30 | kJ/mol | NIST |
| ΔfusH° | 12.39 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [53.10; 57.30] | kJ/mol |
|
| ΔvapH° | 53.10 ± 4.20 | kJ/mol | NIST |
| ΔvapH° | 53.10 | kJ/mol | NIST |
| ΔvapH° | 53.10 ± 4.20 | kJ/mol | NIST |
| ΔvapH° | 57.30 | kJ/mol | NIST |
| ΔvapH° | 57.30 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | 57.30 | kJ/mol | NIST |
| ΔvapH° | 57.30 ± 1.30 | kJ/mol | NIST |
| IE | [10.60; 10.78] | eV |
|
| IE | 10.60 | eV | NIST |
| IE | 10.60 | eV | NIST |
| IE | 10.60 | eV | NIST |
| IE | 10.78 | eV | NIST |
| log10WS | 0.45 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.257 | Crippen Calculated Property | |
| McVol | 56.270 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 3 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | [5242.73; 5674.20] | kPa |
|
| Pc | 5674.20 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 5664.07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 5670.00 | kPa | KDB |
| Pc | 5242.73 ± 100.00 | kPa | NIST |
| Ptriple | 0.26 | kPa | ChemSep v8.3 pure component data Compiled value |
| Tboil | [412.20; 414.80] | K |
|
| Tboil | 414.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 414.00 | K | KDB |
| Tboil | 412.20 | K | NIST |
| Tboil | 414.80 | K | NIST |
| Tboil | 414.45 | K | NIST |
| Tc | [615.00; 654.15] | K |
|
| Tc | 615.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 654.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 615.00 | K | KDB |
| Tc | 616.57 ± 3.00 | K | NIST |
| Tfus | [285.00; 290.00] | K |
|
| Tfus | 286.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 286.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 285.00 | K | KDB |
| Tfus | 285.70 | K | NIST |
| Tfus | 285.70 ± 0.20 | K | NIST |
| Tfus | 285.45 | K | NIST |
| Tfus | 285.30 ± 0.60 | K | NIST |
| Tfus | 285.45 ± 0.50 | K | NIST |
| Tfus | Outlier 290.00 ± 1.00 | K | NIST |
| Ttriple | 286.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 2.40 | ChemSep v8.3 pure component data Compiled value | |
| URi | 2.65 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.210; 0.211] | m3/kmol |
|
| Vc | 0.210 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.211 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.210 | m3/kmol | KDB |
| Zc | [0.2300000; 0.2328580] |
|
|
| Zc | 0.2300000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2328580 | KDB | |
| Zra | 0.23 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [144.20; 145.70] | J/mol×K | [298.15; 300.00] |
|
| Cp,liquid | 144.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 145.70 | J/mol×K | 300.00 | NIST |
| ΔfusH | [9.51; 11.16] | kJ/mol | [285.50; 285.70] |
|
| ΔfusH | 11.16 | kJ/mol | 285.50 | NIST |
| ΔfusH | 11.16 | kJ/mol | 285.50 | NIST |
| ΔfusH | 9.51 | kJ/mol | 285.70 | NIST |
| ΔvapH | [32.70; 46.02] | kJ/mol | [318.00; 414.00] |
|
| ΔvapH | 32.70 | kJ/mol | 318.00 | NIST |
| ΔvapH | 45.30 | kJ/mol | 377.50 | NIST |
| ΔvapH | 46.02 | kJ/mol | 414.00 | KDB |
| Pvap | 20.00 | kPa | 368.40 | Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa |
| ρl | [1051.00; 1059.17] | kg/m3 | [293.00; 298.15] |
|
| ρl | 1051.00 | kg/m3 | 293.00 | KDB |
| ρl | 1051.22 | kg/m3 | 293.15 | Measurements and Comparative Study of Ternary Liquid Liquid Equilibria for Water + Acrylic Acid + Cyclopentyl Methyl Ether at (293.15, 303.15, and 313.15) K and 100.249 kPa |
| ρl | 1059.17 | kg/m3 | 298.15 | Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water |
| ΔfusS | 33.30 | J/mol×K | 285.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [69.23; 174.45] | J/mol×K | [250.00; 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 | 4.99160e+01 | |||
| Coefficient B | -5.89600e+02 | |||
| Coefficient C | 5.35124e+00 | |||
| Coefficient D | -1.35360e-04 | |||
| Coefficient E | 3.08550e-08 | |||
| Temperature range, min. | 250.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 69.23 | J/mol×K | 250.00 | Calculated Property |
| Cp,gas | 94.05 | J/mol×K | 388.89 | Calculated Property |
| Cp,gas | 114.71 | J/mol×K | 527.78 | Calculated Property |
| Cp,gas | 130.58 | J/mol×K | 666.67 | Calculated Property |
| Cp,gas | 142.70 | J/mol×K | 805.56 | Calculated Property |
| Cp,gas | 152.09 | J/mol×K | 944.44 | Calculated Property |
| Cp,gas | 159.49 | J/mol×K | 1083.33 | Calculated Property |
| Cp,gas | 165.44 | J/mol×K | 1222.22 | Calculated Property |
| Cp,gas | 170.34 | J/mol×K | 1361.11 | Calculated Property |
| Cp,gas | 174.45 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [143.00; 167.07] | J/mol×K | [252.65; 375.00] |
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 | 1.42250e+02 | |||
| Coefficient B | 1.83710e+03 | |||
| Coefficient C | -4.52808e+01 | |||
| Coefficient D | 2.17630e-01 | |||
| Coefficient E | -2.70350e-04 | |||
| Temperature range, min. | 252.65 | |||
| Temperature range, max. | 375.00 | |||
| Cp,liquid | 143.00 | J/mol×K | 252.65 | Calculated Property |
| Cp,liquid | 143.74 | J/mol×K | 266.24 | Calculated Property |
| Cp,liquid | 145.01 | J/mol×K | 279.84 | Calculated Property |
| Cp,liquid | 147.02 | J/mol×K | 293.43 | Calculated Property |
| Cp,liquid | 149.91 | J/mol×K | 307.03 | Calculated Property |
| Cp,liquid | 153.66 | J/mol×K | 320.62 | Calculated Property |
| Cp,liquid | 157.94 | J/mol×K | 334.22 | Calculated Property |
| Cp,liquid | 162.14 | J/mol×K | 347.81 | Calculated Property |
| Cp,liquid | 165.44 | J/mol×K | 361.41 | Calculated Property |
| Cp,liquid | 167.07 | J/mol×K | 375.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0013949; 0.0001112] | Pa×s | [286.15; 554.00] |
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 | -1.13670e+02 | |||
| Coefficient B | 5.52660e+03 | |||
| Coefficient C | 1.57500e+01 | |||
| Coefficient D | -1.59830e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 286.15 | |||
| Temperature range, max. | 554.00 | |||
| η | 0.0013949 | Pa×s | 286.15 | Calculated Property |
| η | 0.0008068 | Pa×s | 315.91 | Calculated Property |
| η | 0.0005392 | Pa×s | 345.67 | Calculated Property |
| η | 0.0003957 | Pa×s | 375.43 | Calculated Property |
| η | 0.0003078 | Pa×s | 405.19 | Calculated Property |
| η | 0.0002479 | Pa×s | 434.96 | Calculated Property |
| η | 0.0002031 | Pa×s | 464.72 | Calculated Property |
| η | 0.0001672 | Pa×s | 494.48 | Calculated Property |
| η | 0.0001371 | Pa×s | 524.24 | Calculated Property |
| η | 0.0001112 | Pa×s | 554.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [28.74; 12.82] | kJ/mol | [286.15; 615.00] |
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 | 6.92580e+01 | |||
| Coefficient B | 1.97960e+00 | |||
| Coefficient C | 2.75870e+00 | |||
| Coefficient D | -1.22830e+01 | |||
| Coefficient E | 8.28230e+00 | |||
| Critical temperature, Tc (K) | 6.54150e+02 | |||
| Temperature range, min. | 286.15 | |||
| Temperature range, max. | 615.00 | |||
| ΔvapH | 28.74 | kJ/mol | 286.15 | Calculated Property |
| ΔvapH | 27.74 | kJ/mol | 322.69 | Calculated Property |
| ΔvapH | 27.44 | kJ/mol | 359.23 | Calculated Property |
| ΔvapH | 27.69 | kJ/mol | 395.77 | Calculated Property |
| ΔvapH | 28.27 | kJ/mol | 432.31 | Calculated Property |
| ΔvapH | 28.77 | kJ/mol | 468.84 | Calculated Property |
| ΔvapH | 28.54 | kJ/mol | 505.38 | Calculated Property |
| ΔvapH | 26.54 | kJ/mol | 541.92 | Calculated Property |
| ΔvapH | 21.55 | kJ/mol | 578.46 | Calculated Property |
| ΔvapH | 12.82 | kJ/mol | 615.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.23; 217.66] | kPa | [286.65; 437.98] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.62275e+01 | |||
| Coefficient B | -4.24500e+03 | |||
| Coefficient C | -4.65410e+01 | |||
| Temperature range, min. | 286.65 | |||
| Temperature range, max. | 437.98 | |||
| Pvap | 0.23 | kPa | 286.65 | Calculated Property |
| Pvap | 0.74 | kPa | 303.46 | Calculated Property |
| Pvap | 2.05 | kPa | 320.28 | Calculated Property |
| Pvap | 5.04 | kPa | 337.09 | Calculated Property |
| Pvap | 11.21 | kPa | 353.91 | Calculated Property |
| Pvap | 22.94 | kPa | 370.72 | Calculated Property |
| Pvap | 43.76 | kPa | 387.54 | Calculated Property |
| Pvap | 78.55 | kPa | 404.35 | Calculated Property |
| Pvap | 133.78 | kPa | 421.17 | Calculated Property |
| Pvap | 217.66 | kPa | 437.98 | Calculated Property |
| Pvap | [0.12; 5617.01] | kPa | [276.65; 615.00] |
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 | 4.89587e+01 | |||
| Coefficient B | -7.06289e+03 | |||
| Coefficient C | -4.56415e+00 | |||
| Coefficient D | 1.23864e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 276.65 | |||
| Temperature range, max. | 615.00 | |||
| Pvap | 0.12 | kPa | 276.65 | Calculated Property |
| Pvap | 1.43 | kPa | 314.24 | Calculated Property |
| Pvap | 9.75 | kPa | 351.84 | Calculated Property |
| Pvap | 44.10 | kPa | 389.43 | Calculated Property |
| Pvap | 148.49 | kPa | 427.03 | Calculated Property |
| Pvap | 401.52 | kPa | 464.62 | Calculated Property |
| Pvap | 918.81 | kPa | 502.22 | Calculated Property |
| Pvap | 1847.44 | kPa | 539.81 | Calculated Property |
| Pvap | 3354.92 | kPa | 577.41 | Calculated Property |
| Pvap | 5617.01 | kPa | 615.00 | Calculated Property |
| Pvap | [0.25; 5692.11] | kPa | [286.65; 615.00] |
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 | 5.61842e+01 | |||
| Coefficient B | -7.35729e+03 | |||
| Coefficient C | -5.66895e+00 | |||
| Coefficient D | 2.19318e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 286.65 | |||
| Temperature range, max. | 615.00 | |||
| Pvap | 0.25 | kPa | 286.65 | Calculated Property |
| Pvap | 2.43 | kPa | 323.13 | Calculated Property |
| Pvap | 14.11 | kPa | 359.62 | Calculated Property |
| Pvap | 57.07 | kPa | 396.10 | Calculated Property |
| Pvap | 177.26 | kPa | 432.58 | Calculated Property |
| Pvap | 451.95 | kPa | 469.07 | Calculated Property |
| Pvap | 991.15 | kPa | 505.55 | Calculated Property |
| Pvap | 1933.74 | kPa | 542.03 | Calculated Property |
| Pvap | 3441.24 | kPa | 578.52 | Calculated Property |
| Pvap | 5692.11 | kPa | 615.00 | Calculated Property |
| Pvap | [11.60; 76.87] | kPa | [293.00; 343.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.08131e+01 | |||
| Coefficient B | -1.43054e+03 | |||
| Coefficient C | -1.21929e+02 | |||
| Reference | Gubkov, Fermor, et al., 1964, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 293.00 | |||
| Temperature range, max. | 343.00 | |||
| Pvap | 11.60 | kPa | 293.00 | Calculated Property |
| Pvap | 15.09 | kPa | 298.56 | Calculated Property |
| Pvap | 19.31 | kPa | 304.11 | Calculated Property |
| Pvap | 24.37 | kPa | 309.67 | Calculated Property |
| Pvap | 30.33 | kPa | 315.22 | Calculated Property |
| Pvap | 37.30 | kPa | 320.78 | Calculated Property |
| Pvap | 45.36 | kPa | 326.33 | Calculated Property |
| Pvap | 54.58 | kPa | 331.89 | Calculated Property |
| Pvap | 65.06 | kPa | 337.44 | Calculated Property |
| Pvap | 76.87 | kPa | 343.00 | Calculated Property |
| Pvap | [11.60; 76.87] | kPa | [293.00; 343.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.08131e+01 | |||
| Coefficient B | -1.43054e+03 | |||
| Coefficient C | -1.21929e+02 | |||
| Reference | Gubkov, Fermor, et al., 1964 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 293.00 | |||
| Temperature range, max. | 343.00 | |||
| Pvap | 11.60 | kPa | 293.00 | Calculated Property |
| Pvap | 15.09 | kPa | 298.56 | Calculated Property |
| Pvap | 19.31 | kPa | 304.11 | Calculated Property |
| Pvap | 24.37 | kPa | 309.67 | Calculated Property |
| Pvap | 30.33 | kPa | 315.22 | Calculated Property |
| Pvap | 37.30 | kPa | 320.78 | Calculated Property |
| Pvap | 45.36 | kPa | 326.33 | Calculated Property |
| Pvap | 54.58 | kPa | 331.89 | Calculated Property |
| Pvap | 65.06 | kPa | 337.44 | Calculated Property |
| Pvap | 76.87 | kPa | 343.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1061.14; 565.93] | kg/m3 | [285.15; 597.69] |
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 | 8.31243e+00 | |||
| Coefficient B | 7.86930e-02 | |||
| Coefficient C | 6.54150e+02 | |||
| Coefficient D | 1.69450e-01 | |||
| Temperature range, min. | 285.15 | |||
| Temperature range, max. | 597.69 | |||
| ρl | 1061.14 | kg/m3 | 285.15 | Calculated Property |
| ρl | 1021.25 | kg/m3 | 319.88 | Calculated Property |
| ρl | 979.46 | kg/m3 | 354.60 | Calculated Property |
| ρl | 935.41 | kg/m3 | 389.33 | Calculated Property |
| ρl | 888.60 | kg/m3 | 424.06 | Calculated Property |
| ρl | 838.34 | kg/m3 | 458.78 | Calculated Property |
| ρl | 783.56 | kg/m3 | 493.51 | Calculated Property |
| ρl | 722.58 | kg/m3 | 528.24 | Calculated Property |
| ρl | 652.30 | kg/m3 | 562.96 | Calculated Property |
| ρl | 565.93 | kg/m3 | 597.69 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [286.15; 615.00] |
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 | 3.61160e-04 | |||
| Coefficient B | 2.21600e+03 | |||
| Coefficient C | -2.17990e+01 | |||
| Coefficient D | 5.19470e-02 | |||
| Coefficient E | -5.27930e-05 | |||
| Temperature range, min. | 286.15 | |||
| Temperature range, max. | 615.00 | |||
| γ | 0.03 | N/m | 286.15 | Calculated Property |
| γ | 0.03 | N/m | 322.69 | Calculated Property |
| γ | 0.02 | N/m | 359.23 | Calculated Property |
| γ | 0.02 | N/m | 395.77 | Calculated Property |
| γ | 0.02 | N/m | 432.31 | Calculated Property |
| γ | 0.01 | N/m | 468.84 | Calculated Property |
| γ | 0.01 | N/m | 505.38 | Calculated Property |
| γ | 0.01 | N/m | 541.92 | Calculated Property |
| γ | 0.00 | N/m | 578.46 | Calculated Property |
| γ | 0.00 | N/m | 615.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.07] | W/m×K | [286.15; 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 | 9.24750e-04 | |||
| Coefficient B | 7.03670e-01 | |||
| Coefficient C | 6.26100e+02 | |||
| Coefficient D | 1.12700e+05 | |||
| Temperature range, min. | 286.15 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 286.15 | Calculated Property |
| λgas | 0.02 | W/m×K | 365.47 | Calculated Property |
| λgas | 0.02 | W/m×K | 444.78 | Calculated Property |
| λgas | 0.03 | W/m×K | 524.10 | Calculated Property |
| λgas | 0.04 | W/m×K | 603.42 | Calculated Property |
| λgas | 0.04 | W/m×K | 682.73 | Calculated Property |
| λgas | 0.05 | W/m×K | 762.05 | Calculated Property |
| λgas | 0.06 | W/m×K | 841.37 | Calculated Property |
| λgas | 0.06 | W/m×K | 920.68 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.19; 0.10] | W/m×K | [184.50; 484.50] |
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 | -4.06950e-01 | |||
| Coefficient B | 3.34720e+01 | |||
| Coefficient C | -7.94490e-01 | |||
| Coefficient D | 7.83060e-04 | |||
| Coefficient E | -1.38680e-06 | |||
| Temperature range, min. | 184.50 | |||
| Temperature range, max. | 484.50 | |||
| λliquid | 0.19 | W/m×K | 184.50 | Calculated Property |
| λliquid | 0.18 | W/m×K | 217.83 | Calculated Property |
| λliquid | 0.17 | W/m×K | 251.17 | Calculated Property |
| λliquid | 0.16 | W/m×K | 284.50 | Calculated Property |
| λliquid | 0.15 | W/m×K | 317.83 | Calculated Property |
| λliquid | 0.14 | W/m×K | 351.17 | Calculated Property |
| λliquid | 0.14 | W/m×K | 384.50 | Calculated Property |
| λliquid | 0.13 | W/m×K | 417.83 | Calculated Property |
| λliquid | 0.12 | W/m×K | 451.17 | Calculated Property |
| λliquid | 0.10 | W/m×K | 484.50 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Propenoic acid.
Mixtures
- Urea + 2-Propenoic acid + Water
- 2-Propenoic acid + Cyromazine
- 1-Butanol + 2-Propenoic acid + Water
- Hexanoic acid + 2-Propenoic acid + Water
- 1-Pentanol + 2-Propenoic acid + Water
- Acetic acid, 2-methylpropyl ester + 2-Propenoic acid + Water
- 2-Propenoic acid + Cyclohexane + Water
- Methyl Isobutyl Ketone + 2-Propenoic acid + Water
- Toluene + 2-Propenoic acid + Water
- 2-Propenoic acid + o-Xylene + Water
- p-Xylene + 2-Propenoic acid + Water
- 2-Propenoic acid + Cyclopentane,methoxy- + Water
- Toluene + 2-Propenoic acid
- 2-Propenoic acid + Cyclohexane
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).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- 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
- Crippen Method
- Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
- (Liquid + liquid) equilibria in {water + acrylic acid + (1-butanol, or 2-butanol, or 1-pentanol)} systems at T = 293.2 K, T = 303.2 K, and T = 313.2 K and atmospheric pressure
- Measurement and modelling of urea solubility in aqueous propane-1,2,3-triol and prop-2-enoic acid solutions
- Isobaric Vapor Liquid Liquid Equilibrium for Water + Cyclohexane + Acrylic Acid at 200 mmHg
- Ternary Liquid Liquid Equilibria of Water + Prop-2-enoic Acid + Isobutyl Ethanoate at Different Temperatures
- Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
- Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
- Measurements and Comparative Study of Ternary Liquid Liquid Equilibria for Water + Acrylic Acid + Cyclopentyl Methyl Ether at (293.15, 303.15, and 313.15) K and 100.249 kPa
- Liquid Liquid Equilibria of the Ternary System Water + Acrylic Acid + 4-Methyl-2-pentanone at 298.15 K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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