- InChI
- InChI=1S/C2H2O4/c3-1(4)2(5)6/h(H,3,4)(H,5,6)
- InChI Key
- MUBZPKHOEPUJKR-UHFFFAOYSA-N
- Formula
- C2H2O4
- SMILES
- O=C(O)C(=O)O
- Molecular Weight1
- 90.03
- CAS
- 144-62-7
- Other Names
-
- Acide oxalique
- Acido ossalico
- Aktisal
- Aquisal
- Ethane-1,2-dioic acid
- Ethanedionic acid
- HOOCCOOH
- Kyselina stavelova
- NCI-C55209
- NSC 62774
- Oxaalzuur
- Oxalsaeure
- Oxiric acid
- oxalic acid
- 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).
- 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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- γ : Surface Tension (N/m).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- 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 | 0.9176 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | [-253.50; -242.90] | kJ/mol |
|
| ΔcH°solid | -242.90 ± 0.92 | kJ/mol | NIST |
| ΔcH°solid | -253.50 ± 0.46 | kJ/mol | NIST |
| μ | 2.63 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -661.40 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-733.80; -721.40] | kJ/mol |
|
| ΔfH°gas | -721.40 ± 2.10 | kJ/mol | Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value |
| ΔfH°gas | -733.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°solid | [-829.94; -828.93] | kJ/mol |
|
| ΔfH°solid | -828.93 ± 0.46 | kJ/mol | NIST |
| ΔfH°solid | -829.94 ± 0.96 | kJ/mol | NIST |
| ΔfusH° | 21.22 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 97.91 | kJ/mol | NIST |
| ΔvapH° | 70.68 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [11.20; 11.20] | eV |
|
| IE | 11.20 | eV | NIST |
| IE | 11.20 | eV | NIST |
| IE | 11.20 | eV | NIST |
| log10WS | 0.38 | Aq. Solubility Prediction | |
| logPoct/wat | -0.844 | Crippen Calculated Property | |
| McVol | 53.920 | ml/mol | McGowan Calculated Property |
| Pc | 7020.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 2.15 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | 748.00 | NIST | |
| S°solid,1 bar | 115.60 | J/mol×K | NIST |
| Tboil | 569.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 804.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [374.65; 464.45] | K |
|
| Tfus | 374.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 462.65 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 374.65 | K | Aq. Solubility Prediction |
| Tfus | 464.45 ± 1.50 | K | NIST |
| Tfus | 464.45 ± 1.50 | K | NIST |
| Ttriple | 462.65 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 2.45 | ChemSep v8.3 pure component data Compiled value | |
| URi | 2.60 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.205 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2150000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.21 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | [105.90; 146.00] | J/mol×K | [298.10; 340.00] |
|
| Cp,solid | 120.10 | J/mol×K | 298.10 | NIST |
| Cp,solid | 105.90 | J/mol×K | 298.15 | NIST |
| Cp,solid | 118.00 | J/mol×K | 323.00 | NIST |
| Cp,solid | 146.00 | J/mol×K | 340.00 | NIST |
| ΔsubH | [61.80; 90.60] | kJ/mol | [306.00; 355.50] |
|
| ΔsubH | 61.80 | kJ/mol | 306.00 | NIST |
| ΔsubH | 90.60 | kJ/mol | 355.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [30.01; 65.11] | J/mol×K | [273.00; 1000.10] |
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 | 2.52310e+01 | |||
| Coefficient B | -1.47360e+03 | |||
| Coefficient C | 8.35124e+00 | |||
| Coefficient D | -5.80420e-03 | |||
| Coefficient E | 2.61220e-06 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.10 | |||
| Cp,gas | 30.01 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 36.93 | J/mol×K | 353.79 | Calculated Property |
| Cp,gas | 43.98 | J/mol×K | 434.58 | Calculated Property |
| Cp,gas | 49.63 | J/mol×K | 515.37 | Calculated Property |
| Cp,gas | 53.66 | J/mol×K | 596.16 | Calculated Property |
| Cp,gas | 56.49 | J/mol×K | 676.94 | Calculated Property |
| Cp,gas | 58.62 | J/mol×K | 757.73 | Calculated Property |
| Cp,gas | 60.52 | J/mol×K | 838.52 | Calculated Property |
| Cp,gas | 62.57 | J/mol×K | 919.31 | Calculated Property |
| Cp,gas | 65.11 | J/mol×K | 1000.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [137.30; 180.63] | J/mol×K | [462.65; 603.00] |
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 | 8.19650e+01 | |||
| Coefficient B | -1.96230e+00 | |||
| Coefficient C | 2.17484e+00 | |||
| Coefficient D | 3.88280e-03 | |||
| Coefficient E | 2.16630e-07 | |||
| Temperature range, min. | 462.65 | |||
| Temperature range, max. | 603.00 | |||
| Cp,liquid | 137.30 | J/mol×K | 462.65 | Calculated Property |
| Cp,liquid | 140.95 | J/mol×K | 478.24 | Calculated Property |
| Cp,liquid | 144.84 | J/mol×K | 493.84 | Calculated Property |
| Cp,liquid | 149.00 | J/mol×K | 509.43 | Calculated Property |
| Cp,liquid | 153.44 | J/mol×K | 525.03 | Calculated Property |
| Cp,liquid | 158.19 | J/mol×K | 540.62 | Calculated Property |
| Cp,liquid | 163.25 | J/mol×K | 556.22 | Calculated Property |
| Cp,liquid | 168.67 | J/mol×K | 571.81 | Calculated Property |
| Cp,liquid | 174.45 | J/mol×K | 587.41 | Calculated Property |
| Cp,liquid | 180.63 | J/mol×K | 603.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0008241; 0.0002641] | Pa×s | [428.17; 562.80] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.18578e+01 | |||
| Coefficient B | 2.03664e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 428.17 | |||
| Temperature range, max. | 562.80 | |||
| η | 0.0008241 | Pa×s | 428.17 | Calculated Property |
| η | 0.0007019 | Pa×s | 443.13 | Calculated Property |
| η | 0.0006041 | Pa×s | 458.09 | Calculated Property |
| η | 0.0005248 | Pa×s | 473.05 | Calculated Property |
| η | 0.0004599 | Pa×s | 488.01 | Calculated Property |
| η | 0.0004063 | Pa×s | 502.96 | Calculated Property |
| η | 0.0003614 | Pa×s | 517.92 | Calculated Property |
| η | 0.0003236 | Pa×s | 532.88 | Calculated Property |
| η | 0.0002916 | Pa×s | 547.84 | Calculated Property |
| η | 0.0002641 | Pa×s | 562.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [83.75; 27.80] | kJ/mol | [462.65; 786.03] |
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 | 1.20790e+02 | |||
| Coefficient B | 3.03210e-01 | |||
| Coefficient C | 6.20490e-01 | |||
| Coefficient D | -9.25700e-01 | |||
| Coefficient E | 3.86820e-01 | |||
| Critical temperature, Tc (K) | 8.04000e+02 | |||
| Temperature range, min. | 462.65 | |||
| Temperature range, max. | 786.03 | |||
| ΔvapH | 83.75 | kJ/mol | 462.65 | Calculated Property |
| ΔvapH | 80.11 | kJ/mol | 498.58 | Calculated Property |
| ΔvapH | 76.30 | kJ/mol | 534.51 | Calculated Property |
| ΔvapH | 72.26 | kJ/mol | 570.44 | Calculated Property |
| ΔvapH | 67.89 | kJ/mol | 606.37 | Calculated Property |
| ΔvapH | 63.05 | kJ/mol | 642.31 | Calculated Property |
| ΔvapH | 57.50 | kJ/mol | 678.24 | Calculated Property |
| ΔvapH | 50.81 | kJ/mol | 714.17 | Calculated Property |
| ΔvapH | 42.05 | kJ/mol | 750.10 | Calculated Property |
| ΔvapH | 27.80 | kJ/mol | 786.03 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [448.83; 691.18] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.20464e+01 | |||
| Coefficient B | -3.82034e+03 | |||
| Coefficient C | -1.23938e+02 | |||
| Temperature range, min. | 448.83 | |||
| Temperature range, max. | 691.18 | |||
| Pvap | 1.33 | kPa | 448.83 | Calculated Property |
| Pvap | 3.28 | kPa | 475.76 | Calculated Property |
| Pvap | 7.10 | kPa | 502.69 | Calculated Property |
| Pvap | 13.86 | kPa | 529.61 | Calculated Property |
| Pvap | 24.91 | kPa | 556.54 | Calculated Property |
| Pvap | 41.80 | kPa | 583.47 | Calculated Property |
| Pvap | 66.22 | kPa | 610.40 | Calculated Property |
| Pvap | 99.98 | kPa | 637.32 | Calculated Property |
| Pvap | 144.87 | kPa | 664.25 | Calculated Property |
| Pvap | 202.65 | kPa | 691.18 | Calculated Property |
| Pvap | [2.21; 6997.26] | kPa | [462.65; 804.00] |
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 | 2.10012e+02 | |||
| Coefficient B | -2.09790e+04 | |||
| Coefficient C | -2.70040e+01 | |||
| Coefficient D | 8.63260e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 462.65 | |||
| Temperature range, max. | 804.00 | |||
| Pvap | 2.21 | kPa | 462.65 | Calculated Property |
| Pvap | 11.19 | kPa | 500.58 | Calculated Property |
| Pvap | 41.89 | kPa | 538.51 | Calculated Property |
| Pvap | 124.65 | kPa | 576.43 | Calculated Property |
| Pvap | 311.51 | kPa | 614.36 | Calculated Property |
| Pvap | 681.32 | kPa | 652.29 | Calculated Property |
| Pvap | 1345.75 | kPa | 690.22 | Calculated Property |
| Pvap | 2459.62 | kPa | 728.14 | Calculated Property |
| Pvap | 4239.73 | kPa | 766.07 | Calculated Property |
| Pvap | 6997.26 | kPa | 804.00 | Calculated Property |
| Pvap | [2.15; 7034.56] | kPa | [462.65; 804.00] |
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 | 1.87705e+02 | |||
| Coefficient B | -1.97651e+04 | |||
| Coefficient C | -2.37488e+01 | |||
| Coefficient D | 7.12656e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 462.65 | |||
| Temperature range, max. | 804.00 | |||
| Pvap | 2.15 | kPa | 462.65 | Calculated Property |
| Pvap | 10.91 | kPa | 500.58 | Calculated Property |
| Pvap | 41.14 | kPa | 538.51 | Calculated Property |
| Pvap | 123.58 | kPa | 576.43 | Calculated Property |
| Pvap | 311.75 | kPa | 614.36 | Calculated Property |
| Pvap | 687.16 | kPa | 652.29 | Calculated Property |
| Pvap | 1364.11 | kPa | 690.22 | Calculated Property |
| Pvap | 2496.93 | kPa | 728.14 | Calculated Property |
| Pvap | 4292.86 | kPa | 766.07 | Calculated Property |
| Pvap | 7034.56 | kPa | 804.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1464.97; 439.75] | kg/m3 | [462.65; 804.00] |
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 | 9.45456e+01 | |||
| Coefficient B | 2.15000e-01 | |||
| Coefficient C | 8.04000e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Temperature range, min. | 462.65 | |||
| Temperature range, max. | 804.00 | |||
| ρl | 1464.97 | kg/m3 | 462.65 | Calculated Property |
| ρl | 1407.78 | kg/m3 | 500.58 | Calculated Property |
| ρl | 1347.78 | kg/m3 | 538.51 | Calculated Property |
| ρl | 1284.28 | kg/m3 | 576.43 | Calculated Property |
| ρl | 1216.28 | kg/m3 | 614.36 | Calculated Property |
| ρl | 1142.21 | kg/m3 | 652.29 | Calculated Property |
| ρl | 1059.34 | kg/m3 | 690.22 | Calculated Property |
| ρl | 962.21 | kg/m3 | 728.14 | Calculated Property |
| ρl | 835.93 | kg/m3 | 766.07 | Calculated Property |
| ρl | 439.75 | kg/m3 | 804.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 8.39e-04] | N/m | [462.65; 786.03] |
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 | -1.16120e-02 | |||
| Coefficient B | 8.47010e+02 | |||
| Coefficient C | -7.15080e+00 | |||
| Coefficient D | 9.37950e-03 | |||
| Coefficient E | -9.20180e-06 | |||
| Temperature range, min. | 462.65 | |||
| Temperature range, max. | 786.03 | |||
| γ | 0.04 | N/m | 462.65 | Calculated Property |
| γ | 0.04 | N/m | 498.58 | Calculated Property |
| γ | 0.03 | N/m | 534.51 | Calculated Property |
| γ | 0.02 | N/m | 570.44 | Calculated Property |
| γ | 0.02 | N/m | 606.37 | Calculated Property |
| γ | 0.02 | N/m | 642.31 | Calculated Property |
| γ | 0.01 | N/m | 678.24 | Calculated Property |
| γ | 0.01 | N/m | 714.17 | Calculated Property |
| γ | 0.00 | N/m | 750.10 | Calculated Property |
| γ | 8.39e-04 | N/m | 786.03 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.03] | 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 | 8.48680e-02 | |||
| Coefficient B | 2.34860e-01 | |||
| Coefficient C | 1.54410e+04 | |||
| Coefficient D | 5.07600e+05 | |||
| Temperature range, min. | 274.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | 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 | 0.01 | W/m×K | 516.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 596.67 | Calculated Property |
| λgas | 0.02 | W/m×K | 677.33 | Calculated Property |
| λgas | 0.02 | W/m×K | 758.00 | Calculated Property |
| λgas | 0.02 | W/m×K | 838.67 | Calculated Property |
| λgas | 0.02 | W/m×K | 919.33 | Calculated Property |
| λgas | 0.03 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.18; 0.13] | W/m×K | [462.65; 643.20] |
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 | -8.87750e-02 | |||
| Coefficient B | -2.13560e+02 | |||
| Coefficient C | 1.11800e-01 | |||
| Coefficient D | -2.27250e-03 | |||
| Coefficient E | 3.53010e-07 | |||
| Temperature range, min. | 462.65 | |||
| Temperature range, max. | 643.20 | |||
| λliquid | 0.18 | W/m×K | 462.65 | Calculated Property |
| λliquid | 0.17 | W/m×K | 482.71 | Calculated Property |
| λliquid | 0.17 | W/m×K | 502.77 | Calculated Property |
| λliquid | 0.16 | W/m×K | 522.83 | Calculated Property |
| λliquid | 0.16 | W/m×K | 542.89 | Calculated Property |
| λliquid | 0.15 | W/m×K | 562.96 | Calculated Property |
| λliquid | 0.14 | W/m×K | 583.02 | Calculated Property |
| λliquid | 0.14 | W/m×K | 603.08 | Calculated Property |
| λliquid | 0.13 | W/m×K | 623.14 | Calculated Property |
| λliquid | 0.13 | W/m×K | 643.20 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethanedioic acid.
Mixtures
- Choline chloride + Ethanedioic acid
- Ethanol + Ethanedioic acid
- Ethanedioic acid + Acetic acid
- Ethanedioic acid + Acetone
- Ethanedioic acid + Ethyl Acetate
- Ethanedioic acid + Water
- Ethanedioic acid + 1-Butanol + Water
- Ethanedioic acid + 1-Decanol + Water
- Decanedioic acid, diethyl ester + Ethanedioic acid + Water
- Methyl Isobutyl Ketone + Ethanedioic acid + Water
- Ethanedioic acid + Octane + Water
- 4-Heptanone, 2,6-dimethyl- + Ethanedioic acid + Water
Sources
- KDB Vapor Pressure Data
- Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
- 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
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- An odd-even effect on solubility of dicarboxylic acids in organic solvents
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- Surface Tensions and Densities of Oxalic, Malonic, Succinic, Maleic, Malic, and cis-Pinonic Acids
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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