- InChI
- InChI=1S/C7H6O/c8-6-7-4-2-1-3-5-7/h1-6H
- InChI Key
- HUMNYLRZRPPJDN-UHFFFAOYSA-N
- Formula
- C7H6O
- SMILES
- O=Cc1ccccc1
- Molecular Weight1
- 106.12
- CAS
- 100-52-7
- Other Names
-
- Almond artificial essential oil
- Artifical essential oil of almond
- Artificial Almond Oil
- Artificial bitter almond oil
- Artificial essential oil of almond
- Benzaldehyde FFC
- Benzene carbaldehyde
- Benzenemethylal
- Benzoyl hydride
- Benzyaldehyde
- Benzylaldehyde
- Ethereal oil of bitter almonds
- NA 1989
- NCI-C56133
- NSC 7917
- Oil of Bitter Almond
- Phenylmethanal benzenecarboxaldehyde
- benzenecarbonal
- benzenecarboxaldehyde
- benzoic aldehyde
- phenylmethanal
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- 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).
- EA : Electron affinity (eV).
- SProt : Protonation entropy at 298K (J/mol×K).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open 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.
- 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.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.3127; 0.3200] |
|
|
| ω | 0.3200 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3127 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.3160 | KDB | |
| PAff | [831.70; 834.00] | kJ/mol |
|
| PAff | 834.00 | kJ/mol | NIST |
| PAff | 831.70 ± 1.30 | kJ/mol | NIST |
| Tig | 465.37 | K | KDB |
| BasG | [802.10; 802.50] | kJ/mol |
|
| BasG | 802.10 | kJ/mol | NIST |
| BasG | 802.50 ± 3.40 | kJ/mol | NIST |
| ΔcH°liquid | [-3529.00; -3525.00] | kJ/mol |
|
| ΔcH°liquid | -3525.00 ± 2.00 | kJ/mol | NIST |
| ΔcH°liquid | -3529.00 ± 0.80 | kJ/mol | NIST |
| ΔcH°liquid | -3526.00 | kJ/mol | NIST |
| μ | [2.80; 2.80] | debye |
|
| μ | 2.80 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 2.80 | debye | KDB |
| EA | [0.39; 0.43] | eV |
|
| EA | 0.43 ± 0.01 | eV | NIST |
| EA | 0.42 ± 0.01 | eV | NIST |
| EA | 0.39 ± 0.05 | eV | NIST |
| SProt | 11.00 | J/mol×K | NIST |
| Tflash,cc | 347.04 | K | KDB |
| Tflash,oc | 337.59 | K | KDB |
| ΔfG° | [22.39; 22.40] | kJ/mol |
|
| ΔfG° | 22.39 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 22.40 | kJ/mol | KDB |
| ΔfH°gas | [-40.40; -33.26] | kJ/mol |
|
| ΔfH°gas | -37.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -36.80 | kJ/mol | KDB |
| ΔfH°gas | -36.80 ± 3.00 | kJ/mol | NIST |
| ΔfH°gas | -33.26 | kJ/mol | NIST |
| ΔfH°gas | -37.20 ± 0.92 | kJ/mol | NIST |
| ΔfH°gas | -37.00 ± 4.20 | kJ/mol | NIST |
| ΔfH°gas | -40.40 | kJ/mol | NIST |
| ΔfH°liquid | [-87.10; -83.05] | kJ/mol |
|
| ΔfH°liquid | -87.10 ± 2.20 | kJ/mol | NIST |
| ΔfH°liquid | -83.05 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | -86.20 | kJ/mol | NIST |
| ΔfusH° | 10.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [40.90; 50.30] | kJ/mol |
|
| ΔvapH° | 49.00 ± 0.70 | kJ/mol | NIST |
| ΔvapH° | 49.10 | kJ/mol | NIST |
| ΔvapH° | 50.30 | kJ/mol | NIST |
| ΔvapH° | 50.30 | kJ/mol | NIST |
| ΔvapH° | 49.80 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 45.90 | kJ/mol | NIST |
| ΔvapH° | Outlier 40.90 | kJ/mol | NIST |
| IE | [9.35; 10.00] | eV |
|
| IE | 9.50 ± 0.08 | eV | NIST |
| IE | 9.35 | eV | NIST |
| IE | 9.49 | eV | NIST |
| IE | 9.65 | eV | NIST |
| IE | 9.49 | eV | NIST |
| IE | 9.40 | eV | NIST |
| IE | 9.74 | eV | NIST |
| IE | 9.50 ± 0.02 | eV | NIST |
| IE | 9.53 ± 0.03 | eV | NIST |
| IE | 9.53 ± 0.03 | eV | NIST |
| IE | 9.60 | eV | NIST |
| IE | 9.51 ± 0.02 | eV | NIST |
| IE | 9.60 ± 0.02 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.57 | eV | NIST |
| IE | 9.54 | eV | NIST |
| IE | Outlier 10.00 | eV | NIST |
| IE | 9.80 | eV | NIST |
| log10WS | [-1.25; -1.19] |
|
|
| log10WS | -1.25 | Aq. Solubility Prediction | |
| log10WS | -1.19 | Estimated Solubility | |
| logPoct/wat | 1.499 | Crippen Calculated Property | |
| McVol | 87.300 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [2178.49; 4700.00] | kPa |
|
| Pc | 4410.00 | kPa | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Pc | 4700.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 4660.95 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4650.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 4650.00 | kPa | KDB |
| Pc | 4650.00 ± 46.46 | kPa | NIST |
| Pc | Outlier 2178.49 ± 303.98 | kPa | NIST |
| Pc | 4650.00 ± 46.46 | kPa | NIST |
| Ptriple | 4.84e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [143.60; 1005.00] |
|
|
| Inp | 939.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 939.30 | NIST | |
| Inp | 930.50 | NIST | |
| Inp | 948.90 | NIST | |
| Inp | 924.90 | NIST | |
| Inp | 926.60 | NIST | |
| Inp | 953.40 | NIST | |
| Inp | 950.70 | NIST | |
| Inp | 964.40 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 954.30 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 942.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 960.80 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 927.20 | NIST | |
| Inp | 928.50 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 965.60 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 964.90 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 968.60 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 965.20 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 936.70 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 961.33 | NIST | |
| Inp | 962.09 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 931.30 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 920.90 | NIST | |
| Inp | 960.20 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 944.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 953.70 | NIST | |
| Inp | 953.70 | NIST | |
| Inp | 953.70 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 942.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 944.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 944.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 923.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 913.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 964.90 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 922.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 929.01 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 942.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 919.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 927.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 938.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 954.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 920.42 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 917.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 929.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | Outlier 143.60 | NIST | |
| Inp | Outlier 145.10 | NIST | |
| Inp | Outlier 145.30 | NIST | |
| Inp | Outlier 147.00 | NIST | |
| Inp | 932.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 960.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 963.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 931.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 920.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 940.00 | NIST | |
| Inp | 942.00 | NIST | |
| Inp | 921.00 | NIST | |
| Inp | 936.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 947.00 | NIST | |
| Inp | 925.00 | NIST | |
| Inp | 924.00 | NIST | |
| Inp | 930.00 | NIST | |
| Inp | 939.00 | NIST | |
| Inp | Outlier 145.10 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 949.00 | NIST | |
| Inp | 946.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 934.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 937.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 920.42 | NIST | |
| Inp | 928.00 | NIST | |
| Inp | 955.00 | NIST | |
| Ip | [1470.00; 1569.00] |
|
|
| Ip | Outlier 1568.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1488.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1527.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1494.00 | NIST | |
| Ip | 1515.00 | NIST | |
| Ip | 1486.00 | NIST | |
| Ip | 1512.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1509.00 | NIST | |
| Ip | 1482.00 | NIST | |
| Ip | 1488.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1525.00 | NIST | |
| Ip | 1505.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1498.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1480.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | 1526.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1504.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1497.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1513.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1495.00 | NIST | |
| Ip | Outlier 1563.00 | NIST | |
| Ip | 1525.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1493.00 | NIST | |
| Ip | 1497.00 | NIST | |
| Ip | 1524.00 | NIST | |
| Ip | 1537.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1523.00 | NIST | |
| Ip | 1504.00 | NIST | |
| Ip | 1496.00 | NIST | |
| Ip | 1498.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1513.00 | NIST | |
| Ip | 1494.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1493.00 | NIST | |
| Ip | Outlier 1478.00 | NIST | |
| Ip | 1495.00 | NIST | |
| Ip | 1495.00 | NIST | |
| Ip | 1524.00 | NIST | |
| Ip | 1481.00 | NIST | |
| Ip | 1507.00 | NIST | |
| Ip | 1525.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1504.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1531.00 | NIST | |
| Ip | 1496.00 | NIST | |
| Ip | 1536.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1523.00 | NIST | |
| Ip | 1505.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1539.00 | NIST | |
| Ip | Outlier 1475.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1512.00 | NIST | |
| Ip | 1512.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1496.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1527.00 | NIST | |
| Ip | 1513.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | Outlier 1470.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1527.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1493.00 | NIST | |
| Ip | 1510.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1535.00 | NIST | |
| Ip | 1514.00 | NIST | |
| Ip | Outlier 1473.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1485.00 | NIST | |
| Ip | 1485.00 | NIST | |
| Ip | 1485.00 | NIST | |
| Ip | 1485.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | Outlier 1568.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1535.00 | NIST | |
| Ip | 1542.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | 1497.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1526.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | Outlier 1564.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1514.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1527.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | 1509.00 | NIST | |
| Ip | 1536.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1519.00 | NIST | |
| Ip | 1505.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1525.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1484.00 | NIST | |
| Ip | 1524.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1543.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1537.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | Outlier 1471.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | Outlier 1479.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1524.00 | NIST | |
| Ip | 1499.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1511.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1491.00 | NIST | |
| Ip | 1494.00 | NIST | |
| Ip | 1496.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | 1491.00 | NIST | |
| Ip | 1529.00 | NIST | |
| Ip | 1497.00 | NIST | |
| Ip | 1519.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1527.00 | NIST | |
| Ip | 1527.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1545.00 | NIST | |
| Ip | 1523.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1524.00 | NIST | |
| Ip | 1513.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1536.00 | NIST | |
| Ip | 1494.00 | NIST | |
| Ip | 1539.00 | NIST | |
| Ip | 1539.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1519.00 | NIST | |
| Ip | 1512.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1503.00 | NIST | |
| Ip | 1509.00 | NIST | |
| Ip | Outlier 1561.00 | NIST | |
| Ip | 1510.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | 1539.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1507.00 | NIST | |
| Ip | 1537.00 | NIST | |
| Ip | 1510.00 | NIST | |
| Ip | 1519.00 | NIST | |
| Ip | 1514.00 | NIST | |
| Ip | 1483.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1515.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1514.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1531.00 | NIST | |
| Ip | 1507.00 | NIST | |
| Ip | 1542.00 | NIST | |
| Ip | 1527.00 | NIST | |
| Ip | 1519.00 | NIST | |
| Ip | 1495.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1523.00 | NIST | |
| Ip | 1531.00 | NIST | |
| Ip | 1523.00 | NIST | |
| Ip | 1535.00 | NIST | |
| Ip | Outlier 1479.00 | NIST | |
| Ip | 1494.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1503.00 | NIST | |
| Ip | 1535.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1482.00 | NIST | |
| Ip | 1490.00 | NIST | |
| Ip | Outlier 1477.00 | NIST | |
| Ip | 1482.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1535.00 | NIST | |
| Ip | 1531.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1482.00 | NIST | |
| Ip | 1513.00 | NIST | |
| Ip | Outlier 1476.00 | NIST | |
| Ip | 1504.00 | NIST | |
| Ip | 1482.00 | NIST | |
| Ip | 1490.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1490.00 | NIST | |
| Ip | 1511.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1507.00 | NIST | |
| Ip | 1507.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1489.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1503.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1505.00 | NIST | |
| Ip | Outlier 1479.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1503.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | 1536.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1542.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1524.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1525.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1543.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1493.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | Outlier 1569.00 | NIST | |
| Ip | 1492.00 | NIST | |
| Ip | 1509.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1515.00 | NIST | |
| Ip | 1515.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1511.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1537.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | Outlier 1569.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1485.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1490.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1496.00 | NIST | |
| Ip | 1509.00 | NIST | |
| Ip | 1539.00 | NIST | |
| Ip | 1542.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1525.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1498.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1537.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1490.00 | NIST | |
| Ip | Outlier 1568.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1545.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1510.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1494.00 | NIST | |
| Ip | 1525.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1493.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1532.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1519.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1500.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | 1480.00 | NIST | |
| Ip | 1509.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1513.00 | NIST | |
| Ip | 1517.00 | NIST | |
| Ip | 1516.00 | NIST | |
| Ip | 1507.00 | NIST | |
| Ip | 1509.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | 1518.00 | NIST | |
| Ip | 1503.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1543.00 | NIST | |
| Ip | 1502.00 | NIST | |
| Ip | Outlier 1569.00 | NIST | |
| Ip | 1515.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1485.00 | NIST | |
| Ip | 1542.00 | NIST | |
| Ip | 1498.00 | NIST | |
| Ip | Outlier 1568.00 | NIST | |
| Ip | 1545.00 | NIST | |
| Ip | 1494.00 | NIST | |
| Ip | 1493.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1506.00 | NIST | |
| Ip | 1513.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1480.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1495.00 | NIST | |
| Ip | 1497.00 | NIST | |
| Ip | 1523.00 | NIST | |
| Ip | 1508.00 | NIST | |
| Ip | 1525.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1501.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1512.00 | NIST | |
| Ip | Outlier 1473.00 | NIST | |
| S°liquid | 221.20 | J/mol×K | NIST |
| Tboil | [441.55; 458.15] | K |
|
| Tboil | 452.05 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 452.20 | K | KDB |
| Tboil | 451.20 | K | NIST |
| Tboil | 452.15 ± 0.40 | K | NIST |
| Tboil | 454.90 ± 1.50 | K | NIST |
| Tboil | 458.15 ± 6.00 | K | NIST |
| Tboil | 452.35 ± 1.00 | K | NIST |
| Tboil | 451.15 ± 1.50 | K | NIST |
| Tboil | 452.35 ± 0.40 | K | NIST |
| Tboil | 452.15 ± 2.00 | K | NIST |
| Tboil | Outlier 441.55 ± 1.00 | K | NIST |
| Tboil | 452.25 ± 0.50 | K | NIST |
| Tboil | 452.05 ± 0.60 | K | NIST |
| Tboil | 451.90 ± 0.50 | K | NIST |
| Tboil | 453.15 ± 2.00 | K | NIST |
| Tc | [625.15; 695.00] | K |
|
| Tc | 695.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 695.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 695.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 695.00 | K | KDB |
| Tc | 690.00 ± 20.00 | K | NIST |
| Tc | 695.00 ± 5.00 | K | NIST |
| Tc | Outlier 625.15 ± 3.00 | K | NIST |
| Tc | 695.00 ± 5.00 | K | NIST |
| Tfus | [216.25; 259.70] | K |
|
| Tfus | 216.90 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 247.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 247.00 | K | KDB |
| Tfus | 247.00 | K | NIST |
| Tfus | 216.65 ± 0.50 | K | NIST |
| Tfus | 217.55 ± 0.50 | K | NIST |
| Tfus | 216.25 ± 0.60 | K | NIST |
| Tfus | 259.70 ± 0.50 | K | NIST |
| Ttriple | [216.02; 216.02] | K |
|
| Ttriple | 216.02 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 216.02 ± 0.02 | K | NIST |
| Ttriple | 216.02 ± 0.02 | K | NIST |
| UQi | 3.07 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.02 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.318; 0.324] | m3/kmol |
|
| Vc | 0.318 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.324 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2610000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [335.00; 452.00] | K | [1.30; 100.00] |
|
| Tboilr | 335.20 | K | 1.30 | NIST |
| Tboilr | 335.00 | K | 1.30 | NIST |
| Tboilr | 452.00 | K | 100.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [84.75; 287.55] | J/mol×K | [200.00; 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 | 5.85089e+01 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 5.76721e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 84.75 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 133.37 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 173.46 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 203.66 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 226.58 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 244.38 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 258.54 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 270.04 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 279.55 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 287.55 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [154.43; 213.61] | J/mol×K | [216.02; 451.90] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.22530e+02 | |||
| Coefficient B | 9.83070e-02 | |||
| Coefficient C | 2.28460e-04 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 216.02 | |||
| Temperature range, max. | 451.90 | |||
| Cp,liquid | 154.43 | J/mol×K | 216.02 | Calculated Property |
| Cp,liquid | 159.75 | J/mol×K | 242.23 | Calculated Property |
| Cp,liquid | 165.38 | J/mol×K | 268.44 | Calculated Property |
| Cp,liquid | 171.33 | J/mol×K | 294.65 | Calculated Property |
| Cp,liquid | 177.59 | J/mol×K | 320.86 | Calculated Property |
| Cp,liquid | 184.17 | J/mol×K | 347.06 | Calculated Property |
| Cp,liquid | 191.06 | J/mol×K | 373.27 | Calculated Property |
| Cp,liquid | 198.26 | J/mol×K | 399.48 | Calculated Property |
| Cp,liquid | 205.78 | J/mol×K | 425.69 | Calculated Property |
| Cp,liquid | 213.61 | J/mol×K | 451.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0080393; 0.0003177] | Pa×s | [216.02; 451.90] |
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 | -1.70620e+01 | |||
| Coefficient B | 1.60930e+03 | |||
| Coefficient C | 8.90880e-01 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 216.02 | |||
| Temperature range, max. | 451.90 | |||
| η | 0.0080393 | Pa×s | 216.02 | Calculated Property |
| η | 0.0039761 | Pa×s | 242.23 | Calculated Property |
| η | 0.0022777 | Pa×s | 268.44 | Calculated Property |
| η | 0.0014519 | Pa×s | 294.65 | Calculated Property |
| η | 0.0010027 | Pa×s | 320.86 | Calculated Property |
| η | 0.0007363 | Pa×s | 347.06 | Calculated Property |
| η | 0.0005673 | Pa×s | 373.27 | Calculated Property |
| η | 0.0004542 | Pa×s | 399.48 | Calculated Property |
| η | 0.0003751 | Pa×s | 425.69 | Calculated Property |
| η | 0.0003177 | Pa×s | 451.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [53.73; 0.00] | kJ/mol | [216.02; 695.00] |
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 | 6.19430e+01 | |||
| Coefficient B | 3.81940e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.95000e+02 | |||
| Temperature range, min. | 216.02 | |||
| Temperature range, max. | 695.00 | |||
| ΔvapH | 53.73 | kJ/mol | 216.02 | Calculated Property |
| ΔvapH | 51.37 | kJ/mol | 269.24 | Calculated Property |
| ΔvapH | 48.82 | kJ/mol | 322.46 | Calculated Property |
| ΔvapH | 46.02 | kJ/mol | 375.68 | Calculated Property |
| ΔvapH | 42.93 | kJ/mol | 428.90 | Calculated Property |
| ΔvapH | 39.42 | kJ/mol | 482.12 | Calculated Property |
| ΔvapH | 35.32 | kJ/mol | 535.34 | Calculated Property |
| ΔvapH | 30.25 | kJ/mol | 588.56 | Calculated Property |
| ΔvapH | 23.22 | kJ/mol | 641.78 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 695.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [332.61; 481.36] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46798e+01 | |||
| Coefficient B | -3.99219e+03 | |||
| Coefficient C | -5.52190e+01 | |||
| Temperature range, min. | 332.61 | |||
| Temperature range, max. | 481.36 | |||
| Pvap | 1.33 | kPa | 332.61 | Calculated Property |
| Pvap | 3.00 | kPa | 349.14 | Calculated Property |
| Pvap | 6.17 | kPa | 365.67 | Calculated Property |
| Pvap | 11.83 | kPa | 382.19 | Calculated Property |
| Pvap | 21.28 | kPa | 398.72 | Calculated Property |
| Pvap | 36.28 | kPa | 415.25 | Calculated Property |
| Pvap | 59.02 | kPa | 431.78 | Calculated Property |
| Pvap | 92.18 | kPa | 448.30 | Calculated Property |
| Pvap | 138.87 | kPa | 464.83 | Calculated Property |
| Pvap | 202.66 | kPa | 481.36 | Calculated Property |
| Pvap | [4.84e-05; 4640.01] | kPa | [216.02; 695.00] |
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 | 1.09372e+02 | |||
| Coefficient B | -9.33120e+03 | |||
| Coefficient C | -1.46390e+01 | |||
| Coefficient D | 1.19320e-02 | |||
| Coefficient E | 1.00000e+00 | |||
| Temperature range, min. | 216.02 | |||
| Temperature range, max. | 695.00 | |||
| Pvap | 4.84e-05 | kPa | 216.02 | Calculated Property |
| Pvap | 0.02 | kPa | 269.24 | Calculated Property |
| Pvap | 0.76 | kPa | 322.46 | Calculated Property |
| Pvap | 9.26 | kPa | 375.68 | Calculated Property |
| Pvap | 54.79 | kPa | 428.90 | Calculated Property |
| Pvap | 205.99 | kPa | 482.12 | Calculated Property |
| Pvap | 574.84 | kPa | 535.34 | Calculated Property |
| Pvap | 1310.04 | kPa | 588.56 | Calculated Property |
| Pvap | 2592.33 | kPa | 641.78 | Calculated Property |
| Pvap | 4640.01 | kPa | 695.00 | Calculated Property |
| Pvap | [2.01e-03; 4551.88] | kPa | [247.15; 695.00] |
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 | 6.78778e+01 | |||
| Coefficient B | -8.17952e+03 | |||
| Coefficient C | -7.46624e+00 | |||
| Coefficient D | 2.42851e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 247.15 | |||
| Temperature range, max. | 695.00 | |||
| Pvap | 2.01e-03 | kPa | 247.15 | Calculated Property |
| Pvap | 0.14 | kPa | 296.91 | Calculated Property |
| Pvap | 2.48 | kPa | 346.67 | Calculated Property |
| Pvap | 19.29 | kPa | 396.43 | Calculated Property |
| Pvap | 88.22 | kPa | 446.19 | Calculated Property |
| Pvap | 282.47 | kPa | 495.96 | Calculated Property |
| Pvap | 705.87 | kPa | 545.72 | Calculated Property |
| Pvap | 1477.82 | kPa | 595.48 | Calculated Property |
| Pvap | 2719.96 | kPa | 645.24 | Calculated Property |
| Pvap | 4551.88 | kPa | 695.00 | Calculated Property |
| Pvap | [0.03; 0.69] | kPa | [273.14; 322.06] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.66131e+01 | |||
| Coefficient B | -5.38238e+03 | |||
| Coefficient C | -5.10300e+00 | |||
| Reference | De Maré, Lehman, et al., 1973 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 273.14 | |||
| Temperature range, max. | 322.06 | |||
| Pvap | 0.03 | kPa | 273.14 | Calculated Property |
| Pvap | 0.05 | kPa | 278.58 | Calculated Property |
| Pvap | 0.07 | kPa | 284.01 | Calculated Property |
| Pvap | 0.10 | kPa | 289.45 | Calculated Property |
| Pvap | 0.14 | kPa | 294.88 | Calculated Property |
| Pvap | 0.20 | kPa | 300.32 | Calculated Property |
| Pvap | 0.28 | kPa | 305.75 | Calculated Property |
| Pvap | 0.38 | kPa | 311.19 | Calculated Property |
| Pvap | 0.51 | kPa | 316.62 | Calculated Property |
| Pvap | 0.69 | kPa | 322.06 | Calculated Property |
| Pvap | [0.13; 102.13] | kPa | [299.40; 452.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.35312e+01 | |||
| Coefficient B | -3.17925e+03 | |||
| Coefficient C | -9.49800e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 299.40 | |||
| Temperature range, max. | 452.00 | |||
| Pvap | 0.13 | kPa | 299.40 | Calculated Property |
| Pvap | 0.44 | kPa | 316.36 | Calculated Property |
| Pvap | 1.21 | kPa | 333.31 | Calculated Property |
| Pvap | 2.94 | kPa | 350.27 | Calculated Property |
| Pvap | 6.38 | kPa | 367.22 | Calculated Property |
| Pvap | 12.65 | kPa | 384.18 | Calculated Property |
| Pvap | 23.26 | kPa | 401.13 | Calculated Property |
| Pvap | 40.11 | kPa | 418.09 | Calculated Property |
| Pvap | 65.51 | kPa | 435.04 | Calculated Property |
| Pvap | 102.13 | kPa | 452.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1110.44; 327.59] | kg/m3 | [216.02; 695.00] |
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 | 8.42269e+01 | |||
| Coefficient B | 2.57110e-01 | |||
| Coefficient C | 6.95000e+02 | |||
| Coefficient D | 2.86730e-01 | |||
| Temperature range, min. | 216.02 | |||
| Temperature range, max. | 695.00 | |||
| ρl | 1110.44 | kg/m3 | 216.02 | Calculated Property |
| ρl | 1066.32 | kg/m3 | 269.24 | Calculated Property |
| ρl | 1020.08 | kg/m3 | 322.46 | Calculated Property |
| ρl | 971.20 | kg/m3 | 375.68 | Calculated Property |
| ρl | 918.90 | kg/m3 | 428.90 | Calculated Property |
| ρl | 862.00 | kg/m3 | 482.12 | Calculated Property |
| ρl | 798.43 | kg/m3 | 535.34 | Calculated Property |
| ρl | 724.06 | kg/m3 | 588.56 | Calculated Property |
| ρl | 627.61 | kg/m3 | 641.78 | Calculated Property |
| ρl | 327.59 | kg/m3 | 695.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.02] | N/m | [247.15; 452.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 7.04933e-02 | |||
| Coefficient B | -1.09000e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 247.15 | |||
| Temperature range, max. | 452.15 | |||
| γ | 0.04 | N/m | 247.15 | Calculated Property |
| γ | 0.04 | N/m | 269.93 | Calculated Property |
| γ | 0.04 | N/m | 292.71 | Calculated Property |
| γ | 0.04 | N/m | 315.48 | Calculated Property |
| γ | 0.03 | N/m | 338.26 | Calculated Property |
| γ | 0.03 | N/m | 361.04 | Calculated Property |
| γ | 0.03 | N/m | 383.82 | Calculated Property |
| γ | 0.03 | N/m | 406.59 | Calculated Property |
| γ | 0.02 | N/m | 429.37 | Calculated Property |
| γ | 0.02 | N/m | 452.15 | Calculated Property |
| γ | [0.05; 0.00] | N/m | [216.02; 695.00] |
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 γ in N/m, T in K | |||
| Coefficient A | 7.64090e-02 | |||
| Coefficient B | 1.21790e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.95000e+02 | |||
| Temperature range, min. | 216.02 | |||
| Temperature range, max. | 695.00 | |||
| γ | 0.05 | N/m | 216.02 | Calculated Property |
| γ | 0.04 | N/m | 269.24 | Calculated Property |
| γ | 0.04 | N/m | 322.46 | Calculated Property |
| γ | 0.03 | N/m | 375.68 | Calculated Property |
| γ | 0.02 | N/m | 428.90 | Calculated Property |
| γ | 0.02 | N/m | 482.12 | Calculated Property |
| γ | 0.01 | N/m | 535.34 | Calculated Property |
| γ | 0.01 | N/m | 588.56 | Calculated Property |
| γ | 0.00 | N/m | 641.78 | Calculated Property |
| γ | 0.00 | N/m | 695.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.06] | W/m×K | [451.90; 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 | 2.19990e-04 | |||
| Coefficient B | 8.65200e-01 | |||
| Coefficient C | 2.58160e+02 | |||
| Coefficient D | 1.42430e+05 | |||
| Temperature range, min. | 451.90 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 451.90 | Calculated Property |
| λgas | 0.02 | W/m×K | 512.80 | Calculated Property |
| λgas | 0.03 | W/m×K | 573.70 | Calculated Property |
| λgas | 0.03 | W/m×K | 634.60 | Calculated Property |
| λgas | 0.04 | W/m×K | 695.50 | Calculated Property |
| λgas | 0.04 | W/m×K | 756.40 | Calculated Property |
| λgas | 0.05 | W/m×K | 817.30 | Calculated Property |
| λgas | 0.05 | W/m×K | 878.20 | Calculated Property |
| λgas | 0.06 | W/m×K | 939.10 | Calculated Property |
| λgas | 0.06 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.17; 0.09] | W/m×K | [216.02; 633.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.06550e-01 | |||
| Coefficient B | -1.81320e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 216.02 | |||
| Temperature range, max. | 633.15 | |||
| λliquid | 0.17 | W/m×K | 216.02 | Calculated Property |
| λliquid | 0.16 | W/m×K | 262.37 | Calculated Property |
| λliquid | 0.15 | W/m×K | 308.72 | Calculated Property |
| λliquid | 0.14 | W/m×K | 355.06 | Calculated Property |
| λliquid | 0.13 | W/m×K | 401.41 | Calculated Property |
| λliquid | 0.13 | W/m×K | 447.76 | Calculated Property |
| λliquid | 0.12 | W/m×K | 494.11 | Calculated Property |
| λliquid | 0.11 | W/m×K | 540.45 | Calculated Property |
| λliquid | 0.10 | W/m×K | 586.80 | Calculated Property |
| λliquid | 0.09 | W/m×K | 633.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzaldehyde.
Mixtures
- Diethyl carbonate + Benzaldehyde
- Decane + Benzaldehyde
- Dodecane + Benzaldehyde
- Benzaldehyde + Tetradecane
- Hexadecane + Benzaldehyde
- 2-Propenal, 3-phenyl- + Benzaldehyde
- Toluene + Benzaldehyde + Water
- Carbon dioxide + Benzaldehyde
- Benzaldehyde + Cyclohexane
- Benzoic acid + Benzyl alcohol + Benzaldehyde
- Benzoic acid + Benzaldehyde
- Benzaldehyde + Methyl Alcohol
- Ethanol + Benzaldehyde
- 1-Propanol + Benzaldehyde
- 1-Butanol + Benzaldehyde
- Benzaldehyde + 1-Pentanol
- Benzene, chloro- + Benzaldehyde
- Benzene, nitro- + Benzaldehyde
- Benzaldehyde + Water
- 2-Propanol + Benzaldehyde
Find more mixtures with Benzaldehyde.
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).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- 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.
- 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
- Density, Viscosity, Sound Speed, and Thermoacoustical Parameters of Benzaldehyde with Chlorobenzene or Nitrobenzene at 303.15 K, 308.15 K, and 313.15 K
- High pressure phase equilibrium of carbon dioxide and benzaldehyde binary system
- Isobaric vapor-liquid equilibrium for binary system of cinnamaldehyde + benzaldehyde at 10, 20 and 30 kPa
- Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
- Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
- Liquid-liquid equilibria for ternary system water + toluene+ benzaldehyde at (303.2 to 343.2) K
- Measurement of infinite dilution partition coefficients of isomeric benzene derivatives in [bmim][Tf2N]-CO2 biphasic system and correlation with the ePC-SAFT equation of state
- Densities and excess volumes of binary mixtures of the ionic liquid 1-butyl-3-methylimidazolium hexafluorophosphate with aromatic compound at T = (298.15 to 313.15) K
- Densities and volumetric properties of binary mixtures of the ionic liquid 1-butyl-3-methylimidazolium tetrafluoroborate with benzaldehyde at T = (298.15 to 313.15) K
- Application of the extended real associated solution (ERAS) theory to excess molar enthalpies of benzaldehyde + 1-alkanols (C1 to C5) at T = 298.15 K
- Solubilities of benzoic acid in binary (benzyl alcohol + benzaldehyde) solvent mixtures
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- Thermophysical and optical studies of molecular interactions in binary mixtures of diethyl carbonate with aromatic compounds at temperatures from 298.15 to 323.15 K
- Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
- Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Partition Coefficients of Organic Solutes between Supercritical Carbon Dioxide and Water: Experimental Measurements and Empirical Correlations
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- Limiting Separation Factors and Limiting Activity Coefficients for 2-Furfural, gamma-Nonalactone, Benzaldehyde, and Linalool in Water at 100 deg C
- Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene
- Vapor Pressures, Enthalpies of Vaporization, and Limiting Activity Coefficients in Water at 100 deg C of 2-Furanaldehyde, Benzaldehyde, Phenylethanal, and 2-Phenylethanol
- Activity Coefficients at Infinite Dilution of Volatile Compounds in Water: Effect of Temperature and Salt Concentration
- Liquid Liquid Equilibria for the Ternary System Water + Benzyl Alcohol + Benzaldehyde at (303.2 to 343.2) K
- Solubilities of Benzoic Acid in Binary Methylbenzene + Benzyl Alcohol and Methylbenzene + Benzaldehyde Solvent Mixtures
- Solubilities of Hexanal, Benzaldehyde, 2-Furfural, 2-Phenylethanol, Phenylethanal, and c-Nonalactone in Water at Temperatures between (50 and 100) deg C
- Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
- Density and Viscosity of Acrylonitrile + Cinnamaldehyde, + Anisaldehyde, and + Benzaldehyde at (298.15, 308.15, and 318.15) K
- Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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