- InChI
- InChI=1S/C4H11N/c1-2-3-4-5/h2-5H2,1H3
- InChI Key
- HQABUPZFAYXKJW-UHFFFAOYSA-N
- Formula
- C4H11N
- SMILES
- CCCCN
- Molecular Weight1
- 73.14
- CAS
- 109-73-9
- Other Names
-
- 1-AMINOBUTANE
- 1-Amino-butaan
- 1-Aminobutan
- 1-Butylamine
- BUTYLAMINE
- Butanamine
- Mono-n-butylamine
- Monobutilamina
- Monobutylamine
- N-Butylamin
- NORVALAMINE
- NSC 8029
- Norralamine
- UN 1125
- n-Butilamina
- n-Butylamine
- n-C4H9NH2
- 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).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- 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).
- 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).
- 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.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Vm : Molar Volume (m3/mol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3290 | KDB | |
| PAff | 921.50 | kJ/mol | NIST |
| Tig | 585.37 | K | KDB |
| BasG | 886.60 | kJ/mol | NIST |
| ΔcH°liquid | [-3018.50; -2984.00] | kJ/mol |
|
| ΔcH°liquid | -3018.50 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -2984.00 | kJ/mol | NIST |
| ΔcH°solid | -3018.00 | kJ/mol | NIST |
| μ | 1.30 | debye | KDB |
| η | [0.0004760; 0.0004930] | Pa×s |
|
| η | 0.0004760 | Pa×s | A volum... |
| η | 0.0004930 | Pa×s | Excess ... |
| LFL | 1.70 | % in Air | KDB |
| UFL | 9.80 | % in Air | KDB |
| Tflash,cc | 272.04 | K | KDB |
| Tflash,oc | 260.93 | K | KDB |
| ΔfG° | 49.24 | kJ/mol | KDB |
| ΔfH°gas | [-149.30; -92.11] | kJ/mol |
|
| ΔfH°gas | -92.11 | kJ/mol | KDB |
| ΔfH°gas | -95.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°gas | -149.30 | kJ/mol | NIST |
| ΔfH°liquid | [-182.00; -127.70] | kJ/mol |
|
| ΔfH°liquid | -127.70 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -182.00 | kJ/mol | NIST |
| ΔfusH° | 11.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.14 | kJ/mol | Joback Calculated Property |
| IE | [8.70; 9.40] | eV |
|
| IE | 8.73 ± 0.04 | eV | NIST |
| IE | 8.70 | eV | NIST |
| IE | 8.79 | eV | NIST |
| IE | 8.71 ± 0.03 | eV | NIST |
| IE | 9.40 | eV | NIST |
| log10WS | -0.93 | Crippen Calculated Property | |
| logPoct/wat | 0.745 | Crippen Calculated Property | |
| McVol | 77.200 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [4154.33; 4250.00] | kPa |
|
| Pc | 4250.00 | kPa | KDB |
| Pc | 4200.00 ± 41.96 | kPa | NIST |
| Pc | 4154.33 ± 1.50 | kPa | NIST |
| Inp | [608.00; 629.00] |
|
|
| Inp | 609.40 | NIST | |
| Inp | 609.40 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 629.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 619.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 628.00 | NIST | |
| Inp | 627.00 | NIST | |
| I | [886.00; 918.00] |
|
|
| I | 896.00 | NIST | |
| I | 890.00 | NIST | |
| I | 918.00 | NIST | |
| I | 912.00 | NIST | |
| I | 886.00 | NIST | |
| I | 904.00 | NIST | |
| I | 908.00 | NIST | |
| Tboil | [350.00; 350.15] | K |
|
| Tboil | 350.15 | K | KDB |
| Tboil | 350.00 | K | Evoluti... |
| Tc | [524.00; 531.90] | K |
|
| Tc | 531.90 | K | KDB |
| Tc | 524.00 | K | NIST |
| Tc | 531.90 ± 0.53 | K | NIST |
| Tc | 524.15 ± 1.50 | K | NIST |
| Tfus | [222.65; 224.05] | K |
|
| Tfus | 224.05 | K | KDB |
| Tfus | 224.00 ± 0.10 | K | NIST |
| Tfus | 224.05 | K | NIST |
| Tfus | 222.65 ± 0.50 | K | NIST |
| Vc | 0.277 | m3/kmol | KDB |
| Vm | 9.99e-05 | m3/mol | Thermod... |
| Zc | 0.2661960 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [138.68; 185.91] | J/mol×K | [363.45; 545.13] |
|
| Cp,gas | 138.68 | J/mol×K | 363.45 | Joback Calculated Property |
| Cp,gas | 147.36 | J/mol×K | 393.73 | Joback Calculated Property |
| Cp,gas | 155.70 | J/mol×K | 424.01 | Joback Calculated Property |
| Cp,gas | 163.72 | J/mol×K | 454.29 | Joback Calculated Property |
| Cp,gas | 171.42 | J/mol×K | 484.57 | Joback Calculated Property |
| Cp,gas | 178.82 | J/mol×K | 514.85 | Joback Calculated Property |
| Cp,gas | 185.91 | J/mol×K | 545.13 | Joback Calculated Property |
| Cp,liquid | 188.00 | J/mol×K | 298.15 | NIST |
| η | [0.0003600; 0.0005250] | Pa×s | [293.15; 323.15] |
|
| η | 0.0005250 | Pa×s | 293.15 | Relativ... |
| η | 0.0004960 | Pa×s | 298.15 | Relativ... |
| η | 0.0004440 | Pa×s | 303.15 | Studies... |
| η | 0.0004670 | Pa×s | 303.15 | Relativ... |
| η | 0.0004600 | Pa×s | 303.15 | Density... |
| η | 0.0003930 | Pa×s | 313.15 | Studies... |
| η | 0.0004000 | Pa×s | 313.15 | Density... |
| η | 0.0003600 | Pa×s | 323.15 | Density... |
| ΔvapH | [31.10; 35.50] | kJ/mol | [313.00; 358.00] |
|
| ΔvapH | 34.70 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 35.20 | kJ/mol | 320.50 | NIST |
| ΔvapH | 35.50 | kJ/mol | 322.50 | NIST |
| ΔvapH | 33.50 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 34.70 | kJ/mol | 331.50 | NIST |
| ΔvapH | 32.40 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 32.09 | kJ/mol | 350.10 | KDB |
| ΔvapH | 31.81 | kJ/mol | 350.20 | NIST |
| ΔvapH | 31.10 ± 0.10 | kJ/mol | 358.00 | NIST |
| Pvap | [19.99; 101.33] | kPa | [308.30; 350.00] |
|
| Pvap | 19.99 | kPa | 308.30 | Evoluti... |
| Pvap | 26.66 | kPa | 314.70 | Evoluti... |
| Pvap | 33.33 | kPa | 319.90 | Evoluti... |
| Pvap | 46.66 | kPa | 328.20 | Evoluti... |
| Pvap | 59.99 | kPa | 334.80 | Evoluti... |
| Pvap | 66.66 | kPa | 337.90 | Evoluti... |
| Pvap | 86.66 | kPa | 345.10 | Evoluti... |
| Pvap | 101.33 | kPa | 350.00 | Evoluti... |
| ρl | [709.21; 741.72] | kg/m3 | [288.15; 323.15] |
|
| ρl | 741.72 | kg/m3 | 288.15 | Volumet... |
| ρl | 739.00 | kg/m3 | 293.00 | KDB |
| ρl | 737.12 | kg/m3 | 293.15 | Volumet... |
| ρl | 736.95 | kg/m3 | 293.15 | Volumet... |
| ρl | 737.05 | kg/m3 | 293.15 | Thermod... |
| ρl | 733.30 | kg/m3 | 298.15 | Volumet... |
| ρl | 732.15 | kg/m3 | 298.15 | Volumet... |
| ρl | 732.23 | kg/m3 | 298.15 | Thermod... |
| ρl | 732.18 | kg/m3 | 298.15 | Thermod... |
| ρl | 732.33 | kg/m3 | 298.15 | Volumet... |
| ρl | 733.33 | kg/m3 | 298.15 | Excess ... |
| ρl | 733.33 | kg/m3 | 298.15 | Binary ... |
| ρl | 734.65 | kg/m3 | 298.15 | Volumet... |
| ρl | 728.50 | kg/m3 | 303.15 | Binary ... |
| ρl | 727.51 | kg/m3 | 303.15 | Volumet... |
| ρl | 727.45 | kg/m3 | 303.15 | Thermod... |
| ρl | 728.65 | kg/m3 | 303.15 | Studies... |
| ρl | 727.34 | kg/m3 | 303.15 | Volumet... |
| ρl | 728.65 | kg/m3 | 303.15 | Studies... |
| ρl | 723.67 | kg/m3 | 308.15 | Excess ... |
| ρl | 722.66 | kg/m3 | 308.15 | Volumet... |
| ρl | 723.67 | kg/m3 | 308.15 | Binary ... |
| ρl | 719.17 | kg/m3 | 313.15 | Studies... |
| ρl | 718.66 | kg/m3 | 313.15 | Binary ... |
| ρl | 714.10 | kg/m3 | 318.15 | Binary ... |
| ρl | 714.00 | kg/m3 | 318.15 | Excess ... |
| ρl | 709.21 | kg/m3 | 323.15 | Binary ... |
| csound,fluid | [1205.72; 1296.08] | m/s | [288.15; 308.15] |
|
| csound,fluid | 1296.08 | m/s | 288.15 | Volumet... |
| csound,fluid | 1296.08 | m/s | 288.15 | Densiti... |
| csound,fluid | 1273.56 | m/s | 293.15 | Volumet... |
| csound,fluid | 1273.56 | m/s | 293.15 | Densiti... |
| csound,fluid | 1249.96 | m/s | 298.15 | Volumet... |
| csound,fluid | 1249.96 | m/s | 298.15 | Densiti... |
| csound,fluid | 1228.92 | m/s | 303.15 | Volumet... |
| csound,fluid | 1228.92 | m/s | 303.15 | Densiti... |
| csound,fluid | 1205.72 | m/s | 308.15 | Volumet... |
| csound,fluid | 1205.72 | m/s | 308.15 | Densiti... |
| γ | 0.02 | N/m | 293.20 | KDB |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0004 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [258.47; 373.87] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45389e+01 | |||
| Coefficient B | -3.02088e+03 | |||
| Coefficient C | -4.64950e+01 | |||
| Temperature range, min. | 258.47 | |||
| Temperature range, max. | 373.87 | |||
| Pvap | 1.33 | kPa | 258.47 | Calculated Property |
| Pvap | 3.01 | kPa | 271.29 | Calculated Property |
| Pvap | 6.21 | kPa | 284.11 | Calculated Property |
| Pvap | 11.90 | kPa | 296.94 | Calculated Property |
| Pvap | 21.42 | kPa | 309.76 | Calculated Property |
| Pvap | 36.49 | kPa | 322.58 | Calculated Property |
| Pvap | 59.31 | kPa | 335.40 | Calculated Property |
| Pvap | 92.49 | kPa | 348.23 | Calculated Property |
| Pvap | 139.10 | kPa | 361.05 | Calculated Property |
| Pvap | 202.63 | kPa | 373.87 | Calculated Property |
| Pvap | [0.08; 4205.44] | kPa | [224.05; 531.90] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.84534e+01 | |||
| Coefficient B | -6.04187e+03 | |||
| Coefficient C | -6.30480e+00 | |||
| Coefficient D | 2.90389e-06 | |||
| Temperature range, min. | 224.05 | |||
| Temperature range, max. | 531.90 | |||
| Pvap | 0.08 | kPa | 224.05 | Calculated Property |
| Pvap | 1.27 | kPa | 258.26 | Calculated Property |
| Pvap | 9.42 | kPa | 292.46 | Calculated Property |
| Pvap | 43.36 | kPa | 326.67 | Calculated Property |
| Pvap | 143.05 | kPa | 360.87 | Calculated Property |
| Pvap | 371.25 | kPa | 395.08 | Calculated Property |
| Pvap | 807.37 | kPa | 429.28 | Calculated Property |
| Pvap | 1537.32 | kPa | 463.49 | Calculated Property |
| Pvap | 2644.55 | kPa | 497.69 | Calculated Property |
| Pvap | 4205.44 | kPa | 531.90 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Butanamine.
Mixtures
- 1-Butanamine + Heptane
- 1-Butanamine + Water
- 1-Butanamine + Formamide, N,N-dimethyl-
- 1-Butanamine + N,N-Dimethylacetamide
- Trichloromethane + 1-Butanamine
- 1-Butanamine + Acetonitrile
- 1-Butanamine + Carbon Tetrachloride
- 1-Butanamine + Cyclohexane
- Benzene + 1-Butanamine
- 1-Butanamine + 1-Butanol
- 1-Butanamine + 1,4-Dioxane
- 1-Butanamine + Tetrahydrofuran
- 1-Butanamine + Butane, 1-chloro-
- 1-Butanamine + 1-Propanol, 2-methyl-
- 1-Butanamine + Butane, 1-chloro- + 1-Propanol, 2-methyl-
- 1-Butanamine + Ethanol, 2-methoxy-
- 1-Butanamine + 2-Hexanol
- 3-Hexanol + 1-Butanamine
- 1-Butanamine + 1-Pentanol, 2-methyl-
- 2-Pentanol, 2-methyl- + 1-Butanamine
Find more mixtures with 1-Butanamine.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Volumetric and Acoustic Properties for Binary Mixtures of Dipropylene Glycol Monopropyl Ether with Alkylamines at Temperatures Between 288.15 K and 308.15 K
- Establishing benchmarks for the Second Industrial Fluids Simulation Challenge
- Thermodynamic study of heptane + amine mixtures. V. Excess and solvation Gibbs energies
- Thermodynamics of amide + amine mixtures. 5. Excess molar enthalpies of N,N-dimethylformamide or N,N-dimethylacetamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at 298.15 K. Application of the ERAS model
- Volumetric, acoustic, viscometric, and spectroscopic properties for binary properties for binary mixtures of alkoxypropanol with mono, di-, and tri- alkylamines at a temperature of 298.15K
- Volumetric behaviour of binary mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at p = 0.1 MPa
- Thermodynamic study of (heptane + amine) mixtures. II. Excess and partial molar volumes at 298.15 K
- A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
- Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
- Binary mixtures of ([C4mim][NTf2] + molecular organic solvents): Thermophysical, acoustic and transport properties at various compositions and temperatures
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
- Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents III. Alkylamines in butanols 303.15K
- Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents: IV. Alkylamines in 1,4-dioxane and oxolane at 303.15K
- Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
- Thermodynamics of amide + amine mixtures. 1. Volumetric, speed of sound, and refractive index data for N,Ndimethylformamide + N-propylpropan-1-amine, + N-butylbutan-1-amine, + butan-1-amine, or + hexan-1-amine systems at several temperatures
- Relative Permittivity, Viscosity, and Speed of Sound for 2-Methoxyethanol + Butylamine Mixtures
- Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
- Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
- Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
- Evolution of the Liquid Vapor Equilibrium Properties of Several Unsymmetrical Amines: Determination of Their Binary Isobaric Diagrams and Applications to the Distillation
- Excess Molar Properties for Binary Systems of CnMIM-BF4 Ionic Liquids with Alkylamines in the Temperature Range (298.15 to 318.15) K. Experimental Results and Theoretical Model Calculations
- Densities, Excess Molar Volumes, Speeds of Sound, and Isothermal Compressibilities for 2-(2-Hexyloxyethoxy)ethanol + n-Alkylamine at Temperatures Between 288.15 K and 308.15 K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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