- InChI
- InChI=1S/BrH.H3N/h1H;1H3
- InChI Key
- SWLVFNYSXGMGBS-UHFFFAOYSA-N
- Formula
- NH4Br
- SMILES
- [Br-].[NH4+]
- Molecular Weight1
- 97.94
- CAS
- 12124-97-9
- Other Names
-
- hydrobromic acid monoammoniate
- Cp,solid : Solid phase heat capacity (J/mol×K).
- EA : Electron affinity (eV).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- Pvap : Vapor pressure (kPa).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| EA | 0.67 ± 0.05 | eV | NIST |
| ΔsubH° | 187.90 | kJ/mol | NIST |
Cheméo can also estimate Normal Boiling Point Temperature, Normal melting (fusion) point, Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of formation at standard conditions, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, Ionization energy, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔsubH | 183.70 | kJ/mol | 550.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | [88.66; 92.84] | J/mol×K | [298.00; 411.00] |
NIST
|
| Equation | Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,solid in J/mol×K, T in K | |||
| Coefficient A | 1.57742e+01 | |||
| Coefficient B | 9.82767e+02 | |||
| Coefficient C | -3.03138e+03 | |||
| Coefficient D | 2.87027e+03 | |||
| Coefficient E | -2.37466e+00 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-306.7922, G=-65.09551, H=-271.5424; Data last reviewed in September, 1965 | |||
| Temperature range, min. | 298.00 | |||
| Temperature range, max. | 411.00 | |||
| Cp,solid | 88.66 | J/mol×K | 298.00 | Calculated Property |
| Cp,solid | 89.96 | J/mol×K | 310.56 | Calculated Property |
| Cp,solid | 90.92 | J/mol×K | 323.11 | Calculated Property |
| Cp,solid | 91.58 | J/mol×K | 335.67 | Calculated Property |
| Cp,solid | 92.03 | J/mol×K | 348.22 | Calculated Property |
| Cp,solid | 92.31 | J/mol×K | 360.78 | Calculated Property |
| Cp,solid | 92.48 | J/mol×K | 373.33 | Calculated Property |
| Cp,solid | 92.60 | J/mol×K | 385.89 | Calculated Property |
| Cp,solid | 92.70 | J/mol×K | 398.44 | Calculated Property |
| Cp,solid | 92.84 | J/mol×K | 411.00 | Calculated Property |
| Cp,solid | [72.79; 179.96] | J/mol×K | [411.00; 1500.00] |
NIST
|
| Equation | Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,solid in J/mol×K, T in K | |||
| Coefficient A | -1.25690e+01 | |||
| Coefficient B | 2.57140e+02 | |||
| Coefficient C | -1.23364e+02 | |||
| Coefficient D | 2.50305e+01 | |||
| Coefficient E | -2.06848e-01 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-272.3817, G=42.37179, H=-271.5424; Data last reviewed in September, 1965 | |||
| Temperature range, min. | 411.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,solid | 72.79 | J/mol×K | 411.00 | Calculated Property |
| Cp,solid | 92.35 | J/mol×K | 532.00 | Calculated Property |
| Cp,solid | 109.22 | J/mol×K | 653.00 | Calculated Property |
| Cp,solid | 123.81 | J/mol×K | 774.00 | Calculated Property |
| Cp,solid | 136.44 | J/mol×K | 895.00 | Calculated Property |
| Cp,solid | 147.39 | J/mol×K | 1016.00 | Calculated Property |
| Cp,solid | 156.95 | J/mol×K | 1137.00 | Calculated Property |
| Cp,solid | 165.38 | J/mol×K | 1258.00 | Calculated Property |
| Cp,solid | 172.96 | J/mol×K | 1379.00 | Calculated Property |
| Cp,solid | 179.96 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.13; 101.34] | kPa | [471.45; 669.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.04161e+01 | |||
| Coefficient B | -1.05662e+04 | |||
| Coefficient C | -3.00000e-01 | |||
| Temperature range, min. | 471.45 | |||
| Temperature range, max. | 669.15 | |||
| Pvap | 0.13 | kPa | 471.45 | Calculated Property |
| Pvap | 0.36 | kPa | 493.42 | Calculated Property |
| Pvap | 0.91 | kPa | 515.38 | Calculated Property |
| Pvap | 2.10 | kPa | 537.35 | Calculated Property |
| Pvap | 4.55 | kPa | 559.32 | Calculated Property |
| Pvap | 9.29 | kPa | 581.28 | Calculated Property |
| Pvap | 18.03 | kPa | 603.25 | Calculated Property |
| Pvap | 33.38 | kPa | 625.22 | Calculated Property |
| Pvap | 59.26 | kPa | 647.18 | Calculated Property |
| Pvap | 101.34 | kPa | 669.15 | Calculated Property |
| Pvap | [0.13; 98.92] | kPa | [471.50; 669.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.99540e+01 | |||
| Coefficient B | -1.00907e+04 | |||
| Coefficient C | -1.20450e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 471.50 | |||
| Temperature range, max. | 669.00 | |||
| Pvap | 0.13 | kPa | 471.50 | Calculated Property |
| Pvap | 0.37 | kPa | 493.44 | Calculated Property |
| Pvap | 0.91 | kPa | 515.39 | Calculated Property |
| Pvap | 2.10 | kPa | 537.33 | Calculated Property |
| Pvap | 4.55 | kPa | 559.28 | Calculated Property |
| Pvap | 9.26 | kPa | 581.22 | Calculated Property |
| Pvap | 17.88 | kPa | 603.17 | Calculated Property |
| Pvap | 32.94 | kPa | 625.11 | Calculated Property |
| Pvap | 58.18 | kPa | 647.06 | Calculated Property |
| Pvap | 98.92 | kPa | 669.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ammonium bromide.
Mixtures
- Water + Ammonium bromide
- Propylene Glycol + Water + Ammonium bromide
- 1,3-Propanediol + Water + Ammonium bromide
- 1,4-Butanediol + Water + Ammonium bromide
- 2,3-Butanediol + Water + Ammonium bromide
- Ammonia + Ammonium bromide
- Methyl Alcohol + Water + Ammonium bromide
- d-Arabinose + Water + Ammonium bromide
- D-Arabinitol + Water + Ammonium bromide
- xylose + Water + Ammonium bromide
- Xylitol + Water + Ammonium bromide
- L-Sorbose + Water + Ammonium bromide
- Sorbitol + Water + Ammonium bromide
- Galactose + Water + Ammonium bromide
- Galactitol + Water + Ammonium bromide
- d-Mannose + Water + Ammonium bromide
- D-Mannitol + Water + Ammonium bromide
- Glucose + Water + Ammonium bromide
- Sucrose + Water + Ammonium bromide
Sources
- Cheméo Relay (1.0)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Experimental study of the excess molar volume of ternary mixtures containing {water + (1,2-propanediol, or 1,3-propanediol, or 1,2-butanediol, or 1,3-butanediol, or 1,4-butanediol, or 2,3-butanediol) + electrolytes} at a temperature of 298.15 K and atmospheric pressure
- Salting-in and salting-out effects of organic and inorganic ammonium salts on the aqueous polymer solutions
- Measurement and Correlation of Isothermal Vapor-Liquid Equilibrium Data for the System Methanol + Water + Ammonium Bromide
- Influence of NH4Br on Solvation Behavior of Polyhydroxy Solutes in Aqueous Solutions at Different Temperatures and Atmospheric Pressure
- Vapor Pressures and Liquid Densities of Ammonium Bromide + Ammonia Mixtures
- 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.
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