- 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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 140 150 160 170 180 190 400 450 500 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.50e-4 4.00e-4 4.50e-4 5.00e-4 300 310 320 | ||||
| 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] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 31 32 33 34 35 320 330 340 350 | ||||
| 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] |
|
|
T(K) Vapor pressure (kPa) 20 40 60 80 100 320 340 | ||||
| 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] |
|
|
T(K) Liquid Density (kg/m3) 710 715 720 725 730 735 740 290 300 310 320 | ||||
| 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] |
|
|
T(K) Speed of sound in fluid (m/s) 1200 1220 1240 1260 1280 1300 290 295 300 305 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 500 | ||||
| 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.