- InChI
- InChI=1S/C2H8N2/c3-1-2-4/h1-4H2
- InChI Key
- PIICEJLVQHRZGT-UHFFFAOYSA-N
- Formula
- C2H8N2
- SMILES
- NCCN
- Molecular Weight1
- 60.10
- CAS
- 107-15-3
- Other Names
-
- 1,2-Diamino-ethaan
- 1,2-Diamino-ethano
- 1,2-Diaminoaethan
- 1,2-Diaminoethane
- 1,2-ETHANEDIAMINE
- 1,2-Ethylenediamine
- AETHYLENEDIAMIN
- Aethaldiamin
- BETA-AMINOETHYLAMINE
- Dimethylenediamine
- Ethane-1,2-diamine
- Ethyleendiamine
- Ethylendiamine
- H2NCH2CH2NH2
- NCI-C60402
- UN 1604
- «beta»-Aminoethylamine
- «beta»-Aminoethylamine
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- 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).
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- 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 | 0.5100 | KDB | |
| PAff | [941.80; 951.60] | kJ/mol |
|
| PAff | 951.60 | kJ/mol | NIST |
| PAff | 951.00 ± 4.00 | kJ/mol | NIST |
| PAff | 941.80 | kJ/mol | NIST |
| PAff | 948.10 | kJ/mol | NIST |
| BasG | 912.50 | kJ/mol | NIST |
| ΔcH°liquid | -1867.30 ± 0.50 | kJ/mol | NIST |
| μ | 1.90 | debye | KDB |
| ΔfG° | 98.86 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -17.00 ± 0.59 | kJ/mol | NIST |
| ΔfH°liquid | -63.01 ± 0.54 | kJ/mol | NIST |
| ΔfusH° | 11.33 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [41.60; 54.40] | kJ/mol |
|
| ΔvapH° | 45.01 | kJ/mol | NIST |
| ΔvapH° | 46.00 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 41.60 | kJ/mol | NIST |
| ΔvapH° | 45.69 ± 0.21 | kJ/mol | NIST |
| ΔvapH° | 46.00 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 46.00 | kJ/mol | NIST |
| ΔvapH° | 45.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 44.98 ± 0.12 | kJ/mol | NIST |
| ΔvapH° | Outlier 54.40 ± 1.00 | kJ/mol | NIST |
| IE | [8.60; 9.25] | eV |
|
| IE | 8.60 | eV | NIST |
| IE | 9.25 | eV | NIST |
| log10WS | 0.47 | Crippen Calculated Property | |
| logPoct/wat | -1.096 | Crippen Calculated Property | |
| McVol | 59.000 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 3 | KDB | |
| Pc | [6280.00; 6707.00] | kPa |
|
| Pc | 6280.00 | kPa | KDB |
| Pc | 6650.00 | kPa | Critica... |
| Pc | 6707.00 ± 10.00 | kPa | NIST |
| Inp | [600.00; 625.00] |
|
|
| Inp | 625.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 600.00 | NIST | |
| I | [1183.00; 1265.00] |
|
|
| I | 1195.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1235.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1220.00 | NIST | |
| I | 1233.00 | NIST | |
| I | 1195.00 | NIST | |
| I | 1220.00 | NIST | |
| S°liquid | 202.42 | J/mol×K | NIST |
| Tboil | [389.70; 391.65] | K |
|
| Tboil | 390.40 | K | KDB |
| Tboil | 391.20 | K | NIST |
| Tboil | 390.29 ± 0.30 | K | NIST |
| Tboil | 389.70 | K | NIST |
| Tboil | 390.10 | K | NIST |
| Tboil | 391.65 ± 0.60 | K | NIST |
| Tboil | 390.15 | K | NIST |
| Tc | [593.00; 613.10] | K |
|
| Tc | 593.00 | K | KDB |
| Tc | 613.10 ± 0.30 | K | NIST |
| Tfus | [284.00; 284.15] | K |
|
| Tfus | 284.00 | K | KDB |
| Tfus | 284.15 | K | NIST |
| Ttriple | [284.29; 284.29] | K |
|
| Ttriple | 284.29 | K | KDB |
| Ttriple | 284.29 ± 0.01 | K | NIST |
| Vc | 0.206 | m3/kmol | KDB |
| Zc | 0.2623830 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [113.88; 148.94] | J/mol×K | [390.22; 591.32] |
|
| Cp,gas | 113.88 | J/mol×K | 390.22 | Joback Calculated Property |
| Cp,gas | 120.42 | J/mol×K | 423.74 | Joback Calculated Property |
| Cp,gas | 126.66 | J/mol×K | 457.25 | Joback Calculated Property |
| Cp,gas | 132.63 | J/mol×K | 490.77 | Joback Calculated Property |
| Cp,gas | 138.33 | J/mol×K | 524.29 | Joback Calculated Property |
| Cp,gas | 143.76 | J/mol×K | 557.81 | Joback Calculated Property |
| Cp,gas | 148.94 | J/mol×K | 591.32 | Joback Calculated Property |
| Cp,liquid | [172.34; 178.70] | J/mol×K | [293.15; 353.15] |
|
| Cp,liquid | 172.34 | J/mol×K | 293.15 | Heat Ca... |
| Cp,liquid | 172.43 | J/mol×K | 294.65 | Heat Ca... |
| Cp,liquid | 172.53 | J/mol×K | 296.15 | Heat Ca... |
| Cp,liquid | 172.63 | J/mol×K | 297.65 | Heat Ca... |
| Cp,liquid | 172.59 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 172.66 | J/mol×K | 298.15 | Heat Ca... |
| Cp,liquid | 172.73 | J/mol×K | 299.15 | Heat Ca... |
| Cp,liquid | 172.84 | J/mol×K | 300.65 | Heat Ca... |
| Cp,liquid | 172.95 | J/mol×K | 302.15 | Heat Ca... |
| Cp,liquid | 173.06 | J/mol×K | 303.65 | Heat Ca... |
| Cp,liquid | 173.17 | J/mol×K | 305.15 | Heat Ca... |
| Cp,liquid | 173.29 | J/mol×K | 306.65 | Heat Ca... |
| Cp,liquid | 173.41 | J/mol×K | 308.15 | Heat Ca... |
| Cp,liquid | 173.53 | J/mol×K | 309.65 | Heat Ca... |
| Cp,liquid | 173.66 | J/mol×K | 311.15 | Heat Ca... |
| Cp,liquid | 173.79 | J/mol×K | 312.65 | Heat Ca... |
| Cp,liquid | 178.70 | J/mol×K | 313.00 | NIST |
| Cp,liquid | 173.92 | J/mol×K | 314.15 | Heat Ca... |
| Cp,liquid | 174.05 | J/mol×K | 315.65 | Heat Ca... |
| Cp,liquid | 174.18 | J/mol×K | 317.15 | Heat Ca... |
| Cp,liquid | 174.31 | J/mol×K | 318.65 | Heat Ca... |
| Cp,liquid | 174.45 | J/mol×K | 320.15 | Heat Ca... |
| Cp,liquid | 174.59 | J/mol×K | 321.65 | Heat Ca... |
| Cp,liquid | 174.72 | J/mol×K | 323.15 | Heat Ca... |
| Cp,liquid | 174.86 | J/mol×K | 324.65 | Heat Ca... |
| Cp,liquid | 175.00 | J/mol×K | 326.15 | Heat Ca... |
| Cp,liquid | 175.15 | J/mol×K | 327.65 | Heat Ca... |
| Cp,liquid | 175.29 | J/mol×K | 329.15 | Heat Ca... |
| Cp,liquid | 175.43 | J/mol×K | 330.65 | Heat Ca... |
| Cp,liquid | 175.58 | J/mol×K | 332.15 | Heat Ca... |
| Cp,liquid | 175.72 | J/mol×K | 333.65 | Heat Ca... |
| Cp,liquid | 175.86 | J/mol×K | 335.15 | Heat Ca... |
| Cp,liquid | 176.01 | J/mol×K | 336.65 | Heat Ca... |
| Cp,liquid | 176.15 | J/mol×K | 338.15 | Heat Ca... |
| Cp,liquid | 176.30 | J/mol×K | 339.65 | Heat Ca... |
| Cp,liquid | 176.44 | J/mol×K | 341.15 | Heat Ca... |
| Cp,liquid | 176.59 | J/mol×K | 342.65 | Heat Ca... |
| Cp,liquid | 176.73 | J/mol×K | 344.15 | Heat Ca... |
| Cp,liquid | 176.87 | J/mol×K | 345.65 | Heat Ca... |
| Cp,liquid | 177.02 | J/mol×K | 347.15 | Heat Ca... |
| Cp,liquid | 177.16 | J/mol×K | 348.65 | Heat Ca... |
| Cp,liquid | 177.30 | J/mol×K | 350.15 | Heat Ca... |
| Cp,liquid | 177.44 | J/mol×K | 351.65 | Heat Ca... |
| Cp,liquid | 177.58 | J/mol×K | 353.15 | Heat Ca... |
| η | [0.0011070; 0.0012760] | Pa×s | [298.15; 308.15] |
|
| η | 0.0012760 | Pa×s | 298.15 | Density... |
| η | 0.0012110 | Pa×s | 303.15 | Density... |
| η | 0.0011070 | Pa×s | 308.15 | Density... |
| ΔfusH | [0.49; 22.58] | kJ/mol | [189.00; 284.30] |
|
| ΔfusH | 0.49 | kJ/mol | 189.00 | NIST |
| ΔfusH | 21.08 | kJ/mol | 284.10 | NIST |
| ΔfusH | 22.58 | kJ/mol | 284.20 | NIST |
| ΔfusH | 22.58 | kJ/mol | 284.30 | NIST |
| ΔsubH | 65.60 | kJ/mol | 260.00 | NIST |
| ΔvapH | [37.98; 45.90] | kJ/mol | [344.50; 390.10] |
|
| ΔvapH | 45.60 | kJ/mol | 344.50 | NIST |
| ΔvapH | 43.90 | kJ/mol | 347.00 | NIST |
| ΔvapH | 45.90 | kJ/mol | 351.50 | NIST |
| ΔvapH | 37.98 | kJ/mol | 390.10 | NIST |
| Pvap | [0.66; 43.86] | kPa | [285.50; 365.63] |
|
| Pvap | 0.66 | kPa | 285.50 | Phase e... |
| Pvap | 2.56 | kPa | 305.44 | Phase e... |
| Pvap | 4.48 | kPa | 315.43 | Phase e... |
| Pvap | 4.49 | kPa | 315.48 | Phase e... |
| Pvap | 7.83 | kPa | 326.20 | Phase e... |
| Pvap | 12.41 | kPa | 335.88 | Phase e... |
| Pvap | 19.72 | kPa | 345.70 | Phase e... |
| Pvap | 19.73 | kPa | 345.70 | Phase e... |
| Pvap | 19.74 | kPa | 345.70 | Phase e... |
| Pvap | 19.74 | kPa | 345.70 | Phase e... |
| Pvap | 19.74 | kPa | 345.70 | Phase e... |
| Pvap | 19.73 | kPa | 345.70 | Phase e... |
| Pvap | 29.85 | kPa | 355.67 | Phase e... |
| Pvap | 29.85 | kPa | 355.67 | Phase e... |
| Pvap | 29.83 | kPa | 355.67 | Phase e... |
| Pvap | 29.85 | kPa | 355.67 | Phase e... |
| Pvap | 29.84 | kPa | 355.69 | Phase e... |
| Pvap | 43.82 | kPa | 365.60 | Phase e... |
| Pvap | 43.81 | kPa | 365.60 | Phase e... |
| Pvap | 43.83 | kPa | 365.60 | Phase e... |
| Pvap | 43.86 | kPa | 365.60 | Phase e... |
| Pvap | 43.82 | kPa | 365.63 | Phase e... |
| Pvap | 43.83 | kPa | 365.63 | Phase e... |
| Pvap | 43.81 | kPa | 365.63 | Phase e... |
| ρl | [829.40; 905.99] | kg/m3 | [283.55; 363.15] |
|
| ρl | 905.99 | kg/m3 | 283.55 | Density... |
| ρl | 904.27 | kg/m3 | 285.15 | Volumet... |
| ρl | 903.81 | kg/m3 | 285.65 | Volumet... |
| ρl | 903.34 | kg/m3 | 286.15 | Volumet... |
| ρl | 902.87 | kg/m3 | 286.65 | Volumet... |
| ρl | 902.41 | kg/m3 | 287.15 | Volumet... |
| ρl | 901.94 | kg/m3 | 287.65 | Volumet... |
| ρl | 901.26 | kg/m3 | 288.15 | Volume ... |
| ρl | 901.47 | kg/m3 | 288.15 | Volumet... |
| ρl | 901.00 | kg/m3 | 288.65 | Volumet... |
| ρl | 900.53 | kg/m3 | 289.15 | Volumet... |
| ρl | 900.07 | kg/m3 | 289.65 | Volumet... |
| ρl | 899.60 | kg/m3 | 290.15 | Volumet... |
| ρl | 899.13 | kg/m3 | 290.65 | Volumet... |
| ρl | 898.66 | kg/m3 | 291.15 | Volumet... |
| ρl | 898.19 | kg/m3 | 291.65 | Volumet... |
| ρl | 897.72 | kg/m3 | 292.15 | Volumet... |
| ρl | 897.25 | kg/m3 | 292.65 | Volumet... |
| ρl | 896.00 | kg/m3 | 293.00 | KDB |
| ρl | 897.17 | kg/m3 | 293.06 | Density... |
| ρl | 896.78 | kg/m3 | 293.15 | Volumet... |
| ρl | 896.31 | kg/m3 | 293.65 | Volumet... |
| ρl | 895.85 | kg/m3 | 294.15 | Volumet... |
| ρl | 895.38 | kg/m3 | 294.65 | Volumet... |
| ρl | 894.91 | kg/m3 | 295.15 | Volumet... |
| ρl | 894.44 | kg/m3 | 295.65 | Volumet... |
| ρl | 893.97 | kg/m3 | 296.15 | Volumet... |
| ρl | 893.50 | kg/m3 | 296.65 | Volumet... |
| ρl | 893.03 | kg/m3 | 297.15 | Volumet... |
| ρl | 892.56 | kg/m3 | 297.65 | Volumet... |
| ρl | 895.32 | kg/m3 | 298.15 | PrhoT m... |
| ρl | 893.30 | kg/m3 | 298.15 | Density... |
| ρl | 892.09 | kg/m3 | 298.15 | Volumet... |
| ρl | 891.90 | kg/m3 | 298.15 | Volume ... |
| ρl | 894.79 | kg/m3 | 298.15 | Hydroge... |
| ρl | 892.39 | kg/m3 | 298.15 | Studies... |
| ρl | 892.39 | kg/m3 | 298.15 | Densiti... |
| ρl | 891.62 | kg/m3 | 298.65 | Volumet... |
| ρl | 891.14 | kg/m3 | 299.15 | Volumet... |
| ρl | 890.67 | kg/m3 | 299.65 | Volumet... |
| ρl | 890.20 | kg/m3 | 300.15 | Volumet... |
| ρl | 889.73 | kg/m3 | 300.65 | Volumet... |
| ρl | 889.26 | kg/m3 | 301.15 | Volumet... |
| ρl | 888.79 | kg/m3 | 301.65 | Volumet... |
| ρl | 888.32 | kg/m3 | 302.15 | Volumet... |
| ρl | 888.38 | kg/m3 | 302.40 | Density... |
| ρl | 887.85 | kg/m3 | 302.65 | Volumet... |
| ρl | 890.30 | kg/m3 | 303.15 | Excess ... |
| ρl | 887.38 | kg/m3 | 303.15 | Volumet... |
| ρl | 888.80 | kg/m3 | 303.15 | Density... |
| ρl | 886.90 | kg/m3 | 303.65 | Volumet... |
| ρl | 886.43 | kg/m3 | 304.15 | Volumet... |
| ρl | 885.96 | kg/m3 | 304.65 | Volumet... |
| ρl | 885.49 | kg/m3 | 305.15 | Volumet... |
| ρl | 885.02 | kg/m3 | 305.65 | Volumet... |
| ρl | 884.54 | kg/m3 | 306.15 | Volumet... |
| ρl | 884.07 | kg/m3 | 306.65 | Volumet... |
| ρl | 883.60 | kg/m3 | 307.15 | Volumet... |
| ρl | 883.12 | kg/m3 | 307.65 | Volumet... |
| ρl | 885.63 | kg/m3 | 308.15 | Hydroge... |
| ρl | 882.49 | kg/m3 | 308.15 | Volume ... |
| ρl | 884.90 | kg/m3 | 308.15 | Density... |
| ρl | 882.65 | kg/m3 | 308.15 | Volumet... |
| ρl | 885.90 | kg/m3 | 308.15 | Excess ... |
| ρl | 882.18 | kg/m3 | 308.65 | Volumet... |
| ρl | 881.70 | kg/m3 | 309.15 | Volumet... |
| ρl | 881.23 | kg/m3 | 309.65 | Volumet... |
| ρl | 880.76 | kg/m3 | 310.15 | Volumet... |
| ρl | 880.28 | kg/m3 | 310.65 | Volumet... |
| ρl | 879.81 | kg/m3 | 311.15 | Volumet... |
| ρl | 879.33 | kg/m3 | 311.65 | Volumet... |
| ρl | 878.86 | kg/m3 | 312.15 | Volumet... |
| ρl | 878.38 | kg/m3 | 312.65 | Volumet... |
| ρl | 878.63 | kg/m3 | 312.67 | Density... |
| ρl | 877.91 | kg/m3 | 313.15 | Volumet... |
| ρl | 881.70 | kg/m3 | 313.15 | Excess ... |
| ρl | 880.00 | kg/m3 | 313.15 | Density... |
| ρl | 877.44 | kg/m3 | 313.65 | Volumet... |
| ρl | 876.96 | kg/m3 | 314.15 | Volumet... |
| ρl | 876.48 | kg/m3 | 314.65 | Volumet... |
| ρl | 876.01 | kg/m3 | 315.15 | Volumet... |
| ρl | 875.53 | kg/m3 | 315.65 | Volumet... |
| ρl | 875.06 | kg/m3 | 316.15 | Volumet... |
| ρl | 874.58 | kg/m3 | 316.65 | Volumet... |
| ρl | 874.11 | kg/m3 | 317.15 | Volumet... |
| ρl | 873.63 | kg/m3 | 317.65 | Volumet... |
| ρl | 876.90 | kg/m3 | 318.15 | Excess ... |
| ρl | 873.15 | kg/m3 | 318.15 | Volumet... |
| ρl | 875.20 | kg/m3 | 318.15 | Density... |
| ρl | 867.62 | kg/m3 | 318.15 | Hydroge... |
| ρl | 872.68 | kg/m3 | 318.65 | Volumet... |
| ρl | 872.20 | kg/m3 | 319.15 | Volumet... |
| ρl | 871.72 | kg/m3 | 319.65 | Volumet... |
| ρl | 871.25 | kg/m3 | 320.15 | Volumet... |
| ρl | 870.77 | kg/m3 | 320.65 | Volumet... |
| ρl | 870.29 | kg/m3 | 321.15 | Volumet... |
| ρl | 869.81 | kg/m3 | 321.65 | Volumet... |
| ρl | 869.34 | kg/m3 | 322.15 | Volumet... |
| ρl | 868.86 | kg/m3 | 322.65 | Volumet... |
| ρl | 868.23 | kg/m3 | 323.15 | Volume ... |
| ρl | 868.62 | kg/m3 | 323.15 | Density... |
| ρl | 871.30 | kg/m3 | 323.15 | Excess ... |
| ρl | 868.38 | kg/m3 | 323.15 | Volumet... |
| ρl | 867.90 | kg/m3 | 323.65 | Volumet... |
| ρl | 867.42 | kg/m3 | 324.15 | Volumet... |
| ρl | 866.94 | kg/m3 | 324.65 | Volumet... |
| ρl | 866.47 | kg/m3 | 325.15 | Volumet... |
| ρl | 865.99 | kg/m3 | 325.65 | Volumet... |
| ρl | 865.51 | kg/m3 | 326.15 | Volumet... |
| ρl | 865.03 | kg/m3 | 326.65 | Volumet... |
| ρl | 864.55 | kg/m3 | 327.15 | Volumet... |
| ρl | 864.07 | kg/m3 | 327.65 | Volumet... |
| ρl | 863.59 | kg/m3 | 328.15 | Volumet... |
| ρl | 863.11 | kg/m3 | 328.65 | Volumet... |
| ρl | 862.63 | kg/m3 | 329.15 | Volumet... |
| ρl | 862.14 | kg/m3 | 329.65 | Volumet... |
| ρl | 861.66 | kg/m3 | 330.15 | Volumet... |
| ρl | 861.18 | kg/m3 | 330.65 | Volumet... |
| ρl | 860.70 | kg/m3 | 331.15 | Volumet... |
| ρl | 860.22 | kg/m3 | 331.65 | Volumet... |
| ρl | 859.74 | kg/m3 | 332.15 | Volumet... |
| ρl | 859.25 | kg/m3 | 332.65 | Volumet... |
| ρl | 859.34 | kg/m3 | 332.78 | Density... |
| ρl | 858.77 | kg/m3 | 333.15 | Volumet... |
| ρl | 858.60 | kg/m3 | 333.15 | Volume ... |
| ρl | 858.29 | kg/m3 | 333.65 | Volumet... |
| ρl | 857.81 | kg/m3 | 334.15 | Volumet... |
| ρl | 857.32 | kg/m3 | 334.65 | Volumet... |
| ρl | 856.84 | kg/m3 | 335.15 | Volumet... |
| ρl | 856.36 | kg/m3 | 335.65 | Volumet... |
| ρl | 855.87 | kg/m3 | 336.15 | Volumet... |
| ρl | 855.39 | kg/m3 | 336.65 | Volumet... |
| ρl | 854.91 | kg/m3 | 337.15 | Volumet... |
| ρl | 854.42 | kg/m3 | 337.65 | Volumet... |
| ρl | 853.93 | kg/m3 | 338.15 | Volumet... |
| ρl | 853.45 | kg/m3 | 338.65 | Volumet... |
| ρl | 852.96 | kg/m3 | 339.15 | Volumet... |
| ρl | 852.48 | kg/m3 | 339.65 | Volumet... |
| ρl | 851.99 | kg/m3 | 340.15 | Volumet... |
| ρl | 851.51 | kg/m3 | 340.65 | Volumet... |
| ρl | 851.02 | kg/m3 | 341.15 | Volumet... |
| ρl | 850.53 | kg/m3 | 341.65 | Volumet... |
| ρl | 850.05 | kg/m3 | 342.15 | Volumet... |
| ρl | 849.56 | kg/m3 | 342.65 | Volumet... |
| ρl | 849.65 | kg/m3 | 342.77 | Density... |
| ρl | 849.07 | kg/m3 | 343.15 | Volumet... |
| ρl | 848.58 | kg/m3 | 343.65 | Volumet... |
| ρl | 848.10 | kg/m3 | 344.15 | Volumet... |
| ρl | 847.61 | kg/m3 | 344.65 | Volumet... |
| ρl | 847.12 | kg/m3 | 345.15 | Volumet... |
| ρl | 846.63 | kg/m3 | 345.65 | Volumet... |
| ρl | 846.14 | kg/m3 | 346.15 | Volumet... |
| ρl | 845.66 | kg/m3 | 346.65 | Volumet... |
| ρl | 845.17 | kg/m3 | 347.15 | Volumet... |
| ρl | 844.68 | kg/m3 | 347.65 | Volumet... |
| ρl | 844.19 | kg/m3 | 348.15 | Volumet... |
| ρl | 843.70 | kg/m3 | 348.65 | Volumet... |
| ρl | 843.21 | kg/m3 | 349.15 | Volumet... |
| ρl | 842.72 | kg/m3 | 349.65 | Volumet... |
| ρl | 842.23 | kg/m3 | 350.15 | Volumet... |
| ρl | 841.75 | kg/m3 | 350.65 | Volumet... |
| ρl | 841.26 | kg/m3 | 351.15 | Volumet... |
| ρl | 840.76 | kg/m3 | 351.65 | Volumet... |
| ρl | 840.27 | kg/m3 | 352.15 | Volumet... |
| ρl | 839.78 | kg/m3 | 352.65 | Volumet... |
| ρl | 839.92 | kg/m3 | 352.69 | Density... |
| ρl | 839.29 | kg/m3 | 353.15 | Volumet... |
| ρl | 838.80 | kg/m3 | 353.65 | Volumet... |
| ρl | 838.31 | kg/m3 | 354.15 | Volumet... |
| ρl | 837.81 | kg/m3 | 354.65 | Volumet... |
| ρl | 837.32 | kg/m3 | 355.14 | Volumet... |
| ρl | 836.83 | kg/m3 | 355.65 | Volumet... |
| ρl | 836.33 | kg/m3 | 356.15 | Volumet... |
| ρl | 835.84 | kg/m3 | 356.64 | Volumet... |
| ρl | 835.35 | kg/m3 | 357.15 | Volumet... |
| ρl | 834.85 | kg/m3 | 357.65 | Volumet... |
| ρl | 834.36 | kg/m3 | 358.14 | Volumet... |
| ρl | 833.86 | kg/m3 | 358.64 | Volumet... |
| ρl | 833.37 | kg/m3 | 359.14 | Volumet... |
| ρl | 832.87 | kg/m3 | 359.64 | Volumet... |
| ρl | 832.38 | kg/m3 | 360.14 | Volumet... |
| ρl | 831.88 | kg/m3 | 360.64 | Volumet... |
| ρl | 831.38 | kg/m3 | 361.14 | Volumet... |
| ρl | 830.89 | kg/m3 | 361.65 | Volumet... |
| ρl | 830.39 | kg/m3 | 362.15 | Volumet... |
| ρl | 829.89 | kg/m3 | 362.65 | Volumet... |
| ρl | 829.40 | kg/m3 | 363.15 | Volumet... |
| ΔfusS | [2.57; 79.43] | J/mol×K | [189.00; 284.20] |
|
| ΔfusS | 2.57 | J/mol×K | 189.00 | NIST |
| ΔfusS | 79.43 | J/mol×K | 284.20 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 81.50 | 0.0014 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.64; 202.66] | kPa | [284.29; 413.84] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.55228e+01 | |||
| Coefficient B | -3.66858e+03 | |||
| Coefficient C | -5.45700e+01 | |||
| Temperature range, min. | 284.29 | |||
| Temperature range, max. | 413.84 | |||
| Pvap | 0.64 | kPa | 284.29 | Calculated Property |
| Pvap | 1.64 | kPa | 298.68 | Calculated Property |
| Pvap | 3.79 | kPa | 313.08 | Calculated Property |
| Pvap | 8.00 | kPa | 327.47 | Calculated Property |
| Pvap | 15.70 | kPa | 341.87 | Calculated Property |
| Pvap | 28.87 | kPa | 356.26 | Calculated Property |
| Pvap | 50.22 | kPa | 370.66 | Calculated Property |
| Pvap | 83.27 | kPa | 385.05 | Calculated Property |
| Pvap | 132.34 | kPa | 399.45 | Calculated Property |
| Pvap | 202.66 | kPa | 413.84 | Calculated Property |
| Pvap | [0.67; 6246.95] | kPa | [284.15; 593.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.11320e+02 | |||
| Coefficient B | -9.19093e+03 | |||
| Coefficient C | -1.41955e+01 | |||
| Coefficient D | 1.01223e-05 | |||
| Temperature range, min. | 284.15 | |||
| Temperature range, max. | 593.00 | |||
| Pvap | 0.67 | kPa | 284.15 | Calculated Property |
| Pvap | 5.32 | kPa | 318.47 | Calculated Property |
| Pvap | 26.02 | kPa | 352.78 | Calculated Property |
| Pvap | 90.71 | kPa | 387.10 | Calculated Property |
| Pvap | 248.69 | kPa | 421.42 | Calculated Property |
| Pvap | 573.56 | kPa | 455.73 | Calculated Property |
| Pvap | 1166.85 | kPa | 490.05 | Calculated Property |
| Pvap | 2166.87 | kPa | 524.37 | Calculated Property |
| Pvap | 3766.86 | kPa | 558.68 | Calculated Property |
| Pvap | 6246.95 | kPa | 593.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethylenediamine.
Mixtures
- 1,4-Dioxane + Ethylenediamine
- Ethylenediamine + Water
- 1-Hexanol + Ethylenediamine
- 1-Octanol + Ethylenediamine
- 1-Decanol + Ethylenediamine
- Ethylenediamine + Methyl Alcohol
- Ethanol + Ethylenediamine
- 1-Propanol + Ethylenediamine
- Isopropyl Alcohol + Ethylenediamine
- 1-Butanol + Ethylenediamine
- Ethanol, 2,2'-oxybis- + Ethylenediamine
- 1,2-Ethanediol + Ethylenediamine
- 1-Propanol, 2-methyl- + Ethylenediamine
- 1,2-Ethanediamine, N-ethyl- + Ethylenediamine
- 1,2-Ethanediamine, N-ethyl- + Ethylenediamine + Water
- Ethylenediamine + Triethylenediamine
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Vapor Liquid Equilibrium for Binary Mixtures of 1,4-Diazabicyclo[2.2.2]octane with Ethylenediamine, Ethanolamine, and Ethylene Glycol
- Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
- PrhoT measurement and PC-SAFT modeling of N,N-dimethyl formamide, N -methyl formamide, N,N-dimethyl acetamide, and ethylenediamine from T = (293.15-423.15) K and pressures up to 35 MPa
- Thermodynamic studies of some non-electrolytes in aqueous solutions at low temperatures
- Phase equilibrium properties of binary aqueous solutions containing ethanediamine, 1,2-diaminopropane, 1,3-diaminopropane, or 1,4-diaminobutane at several temperatures
- Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
- Excess molar enthalpies of ethane-1,2-diamine plus primary and secondary alkanols (C1-C4) and correlation with Redlich-Kister, Wilson, NRTL and UNIQUAC models at T = 298 K
- Volumetric properties of the water + ethylenediamine mixture at atmospheric pressure from 288.15 to 353.15K
- Thermochemical study on the Schiff base[H2salen = N,N -bis(salicylidene) ethylendiamine] and its binuclearcopper (II) complex
- Density, viscosity, surface tension, and spectroscopic properties for binary system of 1,2-ethanediamine + diethylene glycol
- Volume properties of liquid mixture of {water (1) + ethylenediamine(2)} over the temperature range from 274.15 to 333.15 K at atmospheric pressure
- Excess Properties for the Binary System of Poly(ethylene glycol) 200 + 1,2-Ethanediamine at T = (303.15 to 323.15) K and the System s Spectroscopic Studies
- Critical Pressures and Temperatures of n-Diaminoalkanes (C2 to C12)
- Density, Viscosity, and Excess Properties for 1,2-Diaminoethane + 1,2-Ethanediol at (298.15, 303.15, and 308.15) K
- Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Ethylenediamine with Alcohols at T = (293.15 to 313.15) K
- Vapor Liquid Equilibrium for Mixtures of Ethylethylenediamine, Ethylenediamine, and Water
- Density for (Water + Ethylenediamine) at Temperatures between (283 and 353) K
- Heat Capacities of Some Liquid a,?-Alkanediamines in the Temperature Range between (293.15 and 353.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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