- InChI
- InChI=1S/C2H7N/c1-2-3/h2-3H2,1H3
- InChI Key
- QUSNBJAOOMFDIB-UHFFFAOYSA-N
- Formula
- C2H7N
- SMILES
- CCN
- Molecular Weight1
- 45.08
- CAS
- 75-04-7
- Other Names
-
- 1-Aminoethane
- Aethylamine
- C2H5NH2
- Etilamina
- Etyloamina
- UN 1036
- aminoethane
- ethanamine
- monoethylamine
- 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).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper 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).
- 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).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- 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 | [0.2760; 0.2890] |
|
|
| ω | 0.2840 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2760 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2890 | KDB | |
| PAff | 912.00 | kJ/mol | NIST |
| Tig | [657.59; 658.15] | K |
|
| Tig | 657.59 | K | KDB |
| Tig | 658.15 | K | NCMS SOLV-DB |
| BasG | 878.00 | kJ/mol | NIST |
| ΔcH°liquid | -1715.00 | kJ/mol | NIST |
| μ | [1.22; 1.30] | debye |
|
| μ | 1.22 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 1.30 | debye | KDB |
| LFL | 3.50 | % in Air | KDB |
| UFL | 14.00 | % in Air | KDB |
| Tflash,cc | [255.15; 255.37] | K |
|
| Tflash,cc | 255.37 | K | KDB |
| Tflash,cc | 255.15 | K | NCMS SOLV-DB |
| ΔfG° | [36.16; 37.30] | kJ/mol |
|
| ΔfG° | 36.16 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 37.30 | kJ/mol | KDB |
| ΔfH°gas | [-57.70; -46.05] | kJ/mol |
|
| ΔfH°gas | -47.15 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -46.05 | kJ/mol | KDB |
| ΔfH°gas | -57.70 | kJ/mol | NIST |
| ΔfH°liquid | -84.50 | kJ/mol | NIST |
| ΔfusH° | 6.13 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 27.32 | kJ/mol | NCMS SOLV-DB |
| IE | [8.70; 9.50] | eV |
|
| IE | 8.90 | eV | NIST |
| IE | 8.70 | eV | NIST |
| IE | 8.80 ± 0.10 | eV | NIST |
| IE | 8.74 | eV | NIST |
| IE | 9.19 | eV | NIST |
| IE | 8.86 ± 0.02 | eV | NIST |
| IE | 9.50 | eV | NIST |
| IE | 9.50 | eV | NIST |
| IE | 9.47 | eV | NIST |
| IE | 9.50 | eV | NIST |
| IE | 9.44 ± 0.18 | eV | NIST |
| IE | 9.50 | eV | NIST |
| log10WS | 0.86 | Relay (1.0) Calculated Property | |
| logPoct/wat | -0.130 | NCMS SOLV-DB | |
| McVol | 49.020 | ml/mol | McGowan Calculated Property |
| NFPA Fire | [%!d(float64=4); %!d(float64=4)] |
|
|
| NFPA Fire | 4 | KDB | |
| NFPA Fire | 4 | NCMS SOLV-DB | |
| NFPA Health | [%!d(float64=3); %!d(float64=3)] |
|
|
| NFPA Health | 3 | KDB | |
| NFPA Health | 3 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | [5600.00; 5631.00] | kPa |
|
| Pc | Outlier 5600.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value |
| Pc | 5623.54 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 5630.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 5631.00 | kPa | Air Liquide Gas Encyclopedia |
| Pc | 5620.00 | kPa | KDB |
| Pc | 5627.59 ± 40.53 | kPa | NIST |
| Ptriple | 0.15 | kPa | ChemSep v8.3 pure component data Compiled value |
| ρc | 243.81 ± 9.92 | kg/m3 | NIST |
| Inp | [370.00; 458.00] |
|
|
| Inp | 390.00 | NIST | |
| Inp | 379.00 | NIST | |
| Inp | 370.00 | NIST | |
| Inp | 458.00 | NIST | |
| Inp | 441.00 | NIST | |
| Inp | 413.00 | NIST | |
| Inp | 413.00 | NIST | |
| Inp | 458.00 | NIST | |
| Inp | 408.00 | NIST | |
| Inp | 410.00 | NIST | |
| Inp | 408.00 | NIST | |
| Inp | 458.00 | NIST | |
| Ip | [712.00; 717.00] |
|
|
| Ip | 717.00 | NIST | |
| Ip | 712.00 | NIST | |
| Ip | 717.00 | NIST | |
| Tboil | [289.70; 292.65] | K |
|
| Tboil | 289.75 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 289.70 | K | KDB |
| Tboil | 289.75 | K | NCMS SOLV-DB |
| Tboil | 289.80 | K | NIST |
| Tboil | 290.15 ± 1.00 | K | NIST |
| Tboil | 289.80 ± 0.20 | K | NIST |
| Tboil | 289.75 ± 0.50 | K | NIST |
| Tboil | 289.75 ± 1.00 | K | NIST |
| Tboil | 289.75 ± 2.00 | K | NIST |
| Tboil | 289.70 ± 0.20 | K | NIST |
| Tboil | 289.75 ± 0.20 | K | NIST |
| Tboil | 289.75 ± 0.20 | K | NIST |
| Tboil | 291.65 ± 2.00 | K | NIST |
| Tboil | 289.70 ± 0.25 | K | NIST |
| Tboil | 289.70 ± 0.20 | K | NIST |
| Tboil | Outlier 292.65 ± 2.00 | K | NIST |
| Tboil | Outlier 292.65 ± 2.00 | K | NIST |
| Tboil | 291.05 ± 2.00 | K | NIST |
| Tboil | 291.85 ± 2.00 | K | NIST |
| Tboil | 291.85 ± 2.00 | K | NIST |
| Tc | [456.00; 456.55] | K |
|
| Tc | 456.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value |
| Tc | 456.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 456.40 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 456.15 | K | Air Liquide Gas Encyclopedia |
| Tc | 456.00 | K | KDB |
| Tc | 456.55 ± 1.00 | K | NIST |
| Tc | 456.35 ± 1.50 | K | NIST |
| Tfus | [187.95; 192.62] | K |
|
| Tfus | 192.05 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 192.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 192.62 | K | KDB |
| Tfus | 192.15 | K | NCMS SOLV-DB |
| Tfus | 192.15 ± 0.30 | K | NIST |
| Tfus | 192.15 ± 0.50 | K | NIST |
| Tfus | 189.90 ± 0.50 | K | NIST |
| Tfus | 192.60 ± 0.12 | K | NIST |
| Tfus | 189.35 ± 1.00 | K | NIST |
| Tfus | Outlier 187.95 ± 2.00 | K | NIST |
| Ttriple | 192.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 2.08 | ChemSep v8.3 pure component data Compiled value | |
| URi | 2.27 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.178; 0.182] | m3/kmol |
|
| Vc | 0.180 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value |
| Vc | 0.178 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.182 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.182 | m3/kmol | KDB |
| Zc | [0.2660000; 0.2697780] |
|
|
| Zc | 0.2660000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 9 Compiled value | |
| Zc | 0.2670000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2697780 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [25.90; 29.10] | kJ/mol | [240.00; 416.50] |
|
| ΔvapH | 28.90 | kJ/mol | 240.00 | NIST |
| ΔvapH | 29.00 | kJ/mol | 255.00 | NIST |
| ΔvapH | 29.10 | kJ/mol | 281.50 | NIST |
| ΔvapH | 28.03 | kJ/mol | 289.80 | KDB |
| ΔvapH | 27.60 | kJ/mol | 339.00 | NIST |
| ΔvapH | 27.20 | kJ/mol | 369.50 | NIST |
| ΔvapH | 25.90 | kJ/mol | 416.50 | NIST |
| Pvap | 0.13 | kPa | 298.15 | NCMS SOLV-DB |
| n0 | 1.36300 | 298.15 | NCMS SOLV-DB | |
| ρl | 683.00 | kg/m3 | 293.00 | KDB |
| γ | [0.02; 0.02] | N/m | [293.20; 298.15] |
|
| γ | 0.02 | N/m | 293.20 | KDB |
| γ | 0.02 | N/m | 298.15 | NCMS SOLV-DB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [60.21; 185.72] | 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 | 5.57620e+01 | |||
| Coefficient B | -8.32710e+02 | |||
| Coefficient C | 5.72424e+00 | |||
| Coefficient D | -3.68450e-04 | |||
| Coefficient E | 1.11470e-07 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 60.21 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 80.12 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 103.58 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 123.85 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 140.07 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 152.92 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 163.25 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 171.80 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 179.15 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 185.72 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [129.79; 144.08] | J/mol×K | [192.15; 348.15] |
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 | 1.29790e+02 | |||
| Coefficient B | -1.23660e+04 | |||
| Coefficient C | -3.79108e+01 | |||
| Coefficient D | 5.37090e-01 | |||
| Coefficient E | -9.14940e-04 | |||
| Temperature range, min. | 192.15 | |||
| Temperature range, max. | 348.15 | |||
| Cp,liquid | 129.79 | J/mol×K | 192.15 | Calculated Property |
| Cp,liquid | 129.79 | J/mol×K | 209.48 | Calculated Property |
| Cp,liquid | 129.79 | J/mol×K | 226.82 | Calculated Property |
| Cp,liquid | 129.79 | J/mol×K | 244.15 | Calculated Property |
| Cp,liquid | 129.79 | J/mol×K | 261.48 | Calculated Property |
| Cp,liquid | 129.82 | J/mol×K | 278.82 | Calculated Property |
| Cp,liquid | 130.22 | J/mol×K | 296.15 | Calculated Property |
| Cp,liquid | 132.79 | J/mol×K | 313.48 | Calculated Property |
| Cp,liquid | 139.34 | J/mol×K | 330.82 | Calculated Property |
| Cp,liquid | 144.08 | J/mol×K | 348.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0017590; 0.0000639] | Pa×s | [192.15; 356.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -4.18530e+01 | |||
| Coefficient B | 1.61950e+03 | |||
| Coefficient C | 5.36490e+00 | |||
| Coefficient D | -3.05630e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 192.15 | |||
| Temperature range, max. | 356.00 | |||
| η | 0.0017590 | Pa×s | 192.15 | Calculated Property |
| η | 0.0011019 | Pa×s | 210.36 | Calculated Property |
| η | 0.0007297 | Pa×s | 228.56 | Calculated Property |
| η | 0.0005010 | Pa×s | 246.77 | Calculated Property |
| η | 0.0003517 | Pa×s | 264.97 | Calculated Property |
| η | 0.0002500 | Pa×s | 283.18 | Calculated Property |
| η | 0.0001786 | Pa×s | 301.38 | Calculated Property |
| η | 0.0001275 | Pa×s | 319.59 | Calculated Property |
| η | 0.0000906 | Pa×s | 337.79 | Calculated Property |
| η | 0.0000639 | Pa×s | 356.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [32.96; 1.78] | kJ/mol | [192.15; 456.15] |
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 | 4.27650e+01 | |||
| Coefficient B | 5.87180e-01 | |||
| Coefficient C | -3.35020e-01 | |||
| Coefficient D | 1.72510e-01 | |||
| Coefficient E | -1.51340e-03 | |||
| Critical temperature, Tc (K) | 4.56400e+02 | |||
| Temperature range, min. | 192.15 | |||
| Temperature range, max. | 456.15 | |||
| ΔvapH | 32.96 | kJ/mol | 192.15 | Calculated Property |
| ΔvapH | 31.40 | kJ/mol | 221.48 | Calculated Property |
| ΔvapH | 29.75 | kJ/mol | 250.82 | Calculated Property |
| ΔvapH | 27.97 | kJ/mol | 280.15 | Calculated Property |
| ΔvapH | 26.00 | kJ/mol | 309.48 | Calculated Property |
| ΔvapH | 23.77 | kJ/mol | 338.82 | Calculated Property |
| ΔvapH | 21.15 | kJ/mol | 368.15 | Calculated Property |
| ΔvapH | 17.91 | kJ/mol | 397.48 | Calculated Property |
| ΔvapH | 13.42 | kJ/mol | 426.82 | Calculated Property |
| ΔvapH | 1.78 | kJ/mol | 456.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 5118.00] | kPa | [224.17; 456.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.33148e+01 | |||
| Coefficient B | -1.74825e+03 | |||
| Coefficient C | -8.99710e+01 | |||
| Temperature range, min. | 224.17 | |||
| Temperature range, max. | 456.15 | |||
| Pvap | 1.33 | kPa | 224.17 | Calculated Property |
| Pvap | 10.88 | kPa | 249.95 | Calculated Property |
| Pvap | 49.55 | kPa | 275.72 | Calculated Property |
| Pvap | 156.00 | kPa | 301.50 | Calculated Property |
| Pvap | 382.84 | kPa | 327.27 | Calculated Property |
| Pvap | 787.94 | kPa | 353.05 | Calculated Property |
| Pvap | 1425.71 | kPa | 378.82 | Calculated Property |
| Pvap | 2340.83 | kPa | 404.60 | Calculated Property |
| Pvap | 3565.31 | kPa | 430.37 | Calculated Property |
| Pvap | 5118.00 | kPa | 456.15 | Calculated Property |
| Pvap | [0.12; 5548.77] | kPa | [190.85; 456.35] |
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 | 1.08618e+02 | |||
| Coefficient B | -6.76422e+03 | |||
| Coefficient C | -1.44391e+01 | |||
| Coefficient D | 1.55603e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 190.85 | |||
| Temperature range, max. | 456.35 | |||
| Pvap | 0.12 | kPa | 190.85 | Calculated Property |
| Pvap | 2.17 | kPa | 220.35 | Calculated Property |
| Pvap | 16.44 | kPa | 249.85 | Calculated Property |
| Pvap | 72.97 | kPa | 279.35 | Calculated Property |
| Pvap | 226.63 | kPa | 308.85 | Calculated Property |
| Pvap | 551.54 | kPa | 338.35 | Calculated Property |
| Pvap | 1133.54 | kPa | 367.85 | Calculated Property |
| Pvap | 2070.79 | kPa | 397.35 | Calculated Property |
| Pvap | 3485.80 | kPa | 426.85 | Calculated Property |
| Pvap | 5548.77 | kPa | 456.35 | Calculated Property |
| Pvap | [0.15; 5561.76] | kPa | [192.15; 456.15] |
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 | 7.23914e+01 | |||
| Coefficient B | -5.54724e+03 | |||
| Coefficient C | -8.69511e+00 | |||
| Coefficient D | 7.84304e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 192.15 | |||
| Temperature range, max. | 456.15 | |||
| Pvap | 0.15 | kPa | 192.15 | Calculated Property |
| Pvap | 2.17 | kPa | 221.48 | Calculated Property |
| Pvap | 15.33 | kPa | 250.82 | Calculated Property |
| Pvap | 67.10 | kPa | 280.15 | Calculated Property |
| Pvap | 211.19 | kPa | 309.48 | Calculated Property |
| Pvap | 526.53 | kPa | 338.82 | Calculated Property |
| Pvap | 1109.32 | kPa | 368.15 | Calculated Property |
| Pvap | 2065.30 | kPa | 397.48 | Calculated Property |
| Pvap | 3507.63 | kPa | 426.82 | Calculated Property |
| Pvap | 5561.76 | kPa | 456.15 | Calculated Property |
| Pvap | [0.13; 101.09] | kPa | [190.80; 289.80] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.48652e+01 | |||
| Coefficient B | -2.58222e+03 | |||
| Coefficient C | -3.78540e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 190.80 | |||
| Temperature range, max. | 289.80 | |||
| Pvap | 0.13 | kPa | 190.80 | Calculated Property |
| Pvap | 0.41 | kPa | 201.80 | Calculated Property |
| Pvap | 1.11 | kPa | 212.80 | Calculated Property |
| Pvap | 2.66 | kPa | 223.80 | Calculated Property |
| Pvap | 5.78 | kPa | 234.80 | Calculated Property |
| Pvap | 11.56 | kPa | 245.80 | Calculated Property |
| Pvap | 21.57 | kPa | 256.80 | Calculated Property |
| Pvap | 37.92 | kPa | 267.80 | Calculated Property |
| Pvap | 63.32 | kPa | 278.80 | Calculated Property |
| Pvap | 101.09 | kPa | 289.80 | Calculated Property |
| Pvap | [101.37; 5006.10] | kPa | [289.80; 449.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50362e+01 | |||
| Coefficient B | -2.77190e+03 | |||
| Coefficient C | -2.37160e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 289.80 | |||
| Temperature range, max. | 449.00 | |||
| Pvap | 101.37 | kPa | 289.80 | Calculated Property |
| Pvap | 194.06 | kPa | 307.49 | Calculated Property |
| Pvap | 344.23 | kPa | 325.18 | Calculated Property |
| Pvap | 573.03 | kPa | 342.87 | Calculated Property |
| Pvap | 904.18 | kPa | 360.56 | Calculated Property |
| Pvap | 1363.24 | kPa | 378.24 | Calculated Property |
| Pvap | 1976.69 | kPa | 395.93 | Calculated Property |
| Pvap | 2771.18 | kPa | 413.62 | Calculated Property |
| Pvap | 3772.72 | kPa | 431.31 | Calculated Property |
| Pvap | 5006.10 | kPa | 449.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [801.12; 271.13] | kg/m3 | [183.15; 456.35] |
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 | 6.15978e+01 | |||
| Coefficient B | 2.52970e-01 | |||
| Coefficient C | 4.56400e+02 | |||
| Coefficient D | 2.79480e-01 | |||
| Temperature range, min. | 183.15 | |||
| Temperature range, max. | 456.35 | |||
| ρl | 801.12 | kg/m3 | 183.15 | Calculated Property |
| ρl | 770.82 | kg/m3 | 213.51 | Calculated Property |
| ρl | 738.97 | kg/m3 | 243.86 | Calculated Property |
| ρl | 705.18 | kg/m3 | 274.22 | Calculated Property |
| ρl | 668.91 | kg/m3 | 304.57 | Calculated Property |
| ρl | 629.28 | kg/m3 | 334.93 | Calculated Property |
| ρl | 584.79 | kg/m3 | 365.28 | Calculated Property |
| ρl | 532.43 | kg/m3 | 395.64 | Calculated Property |
| ρl | 463.97 | kg/m3 | 425.99 | Calculated Property |
| ρl | 271.13 | kg/m3 | 456.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.02] | N/m | [192.15; 289.75] |
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 | 6.01062e-02 | |||
| Coefficient B | -1.37200e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 192.15 | |||
| Temperature range, max. | 289.75 | |||
| γ | 0.03 | N/m | 192.15 | Calculated Property |
| γ | 0.03 | N/m | 202.99 | Calculated Property |
| γ | 0.03 | N/m | 213.84 | Calculated Property |
| γ | 0.03 | N/m | 224.68 | Calculated Property |
| γ | 0.03 | N/m | 235.53 | Calculated Property |
| γ | 0.03 | N/m | 246.37 | Calculated Property |
| γ | 0.02 | N/m | 257.22 | Calculated Property |
| γ | 0.02 | N/m | 268.06 | Calculated Property |
| γ | 0.02 | N/m | 278.91 | Calculated Property |
| γ | 0.02 | N/m | 289.75 | Calculated Property |
| γ | [0.04; 1.11e-05] | N/m | [192.15; 452.98] |
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 | -8.52030e-03 | |||
| Coefficient B | 1.36140e+02 | |||
| Coefficient C | -4.28400e+00 | |||
| Coefficient D | 5.74020e-03 | |||
| Coefficient E | -1.64760e-05 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 456.15 K. | |||
| Temperature range, min. | 192.15 | |||
| Temperature range, max. | 452.98 | |||
| γ | 0.04 | N/m | 192.15 | Calculated Property |
| γ | 0.03 | N/m | 221.13 | Calculated Property |
| γ | 0.03 | N/m | 250.11 | Calculated Property |
| γ | 0.02 | N/m | 279.09 | Calculated Property |
| γ | 0.02 | N/m | 308.08 | Calculated Property |
| γ | 0.01 | N/m | 337.06 | Calculated Property |
| γ | 0.01 | N/m | 366.04 | Calculated Property |
| γ | 0.01 | N/m | 395.02 | Calculated Property |
| γ | 0.00 | N/m | 424.00 | Calculated Property |
| γ | 1.11e-05 | N/m | 452.98 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.11] | W/m×K | [192.15; 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 | 4.06790e-01 | |||
| Coefficient B | 5.16200e-03 | |||
| Coefficient C | 1.28060e+03 | |||
| Coefficient D | 1.72180e+06 | |||
| Temperature range, min. | 192.15 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 192.15 | Calculated Property |
| λgas | 0.02 | W/m×K | 281.91 | Calculated Property |
| λgas | 0.02 | W/m×K | 371.67 | Calculated Property |
| λgas | 0.04 | W/m×K | 461.43 | Calculated Property |
| λgas | 0.05 | W/m×K | 551.19 | Calculated Property |
| λgas | 0.06 | W/m×K | 640.96 | Calculated Property |
| λgas | 0.07 | W/m×K | 730.72 | Calculated Property |
| λgas | 0.08 | W/m×K | 820.48 | Calculated Property |
| λgas | 0.09 | W/m×K | 910.24 | Calculated Property |
| λgas | 0.11 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.21; 0.18] | W/m×K | [192.15; 413.15] |
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 | 1.77440e-01 | |||
| Coefficient B | 5.85820e+02 | |||
| Coefficient C | -1.11650e+01 | |||
| Coefficient D | 4.31820e-02 | |||
| Coefficient E | -9.50240e-05 | |||
| Temperature range, min. | 192.15 | |||
| Temperature range, max. | 413.15 | |||
| λliquid | 0.21 | W/m×K | 192.15 | Calculated Property |
| λliquid | 0.21 | W/m×K | 216.71 | Calculated Property |
| λliquid | 0.20 | W/m×K | 241.26 | Calculated Property |
| λliquid | 0.19 | W/m×K | 265.82 | Calculated Property |
| λliquid | 0.19 | W/m×K | 290.37 | Calculated Property |
| λliquid | 0.18 | W/m×K | 314.93 | Calculated Property |
| λliquid | 0.18 | W/m×K | 339.48 | Calculated Property |
| λliquid | 0.18 | W/m×K | 364.04 | Calculated Property |
| λliquid | 0.18 | W/m×K | 388.59 | Calculated Property |
| λliquid | 0.18 | W/m×K | 413.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethylamine.
Sources
- KDB Vapor Pressure Data
- Air Liquide Gas Encyclopedia
- 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 9 ChEDL chemicals 1.5.2, from Marsh, K. N.; Young, C. L.; Morton, D. W.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 9. Organic Compounds Containing Nitrogen. J. Chem. Eng. Data 2006, 51, 305-314.
- 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.
- 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
- Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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