Phase behavior
|
Triple point
| 195.4 K (–77.75 °C), 6.060 kPa
|
Critical point
| 405.5 K (132.3 °C), 11.300 MPa
|
Std enthalpy change of fusion, ΔfusHo
| +5.653 kJ/mol
|
Std entropy change of fusion, ΔfusSo
| +28.93 J/(mol·K)
|
Std enthalpy change of vaporization, ΔvapHo
| +23.35 kJ/mol at BP of –33.4 °C
|
Std entropy change of vaporization, ΔvapSo
| +97.41 J/(mol·K) at BP of –33.4 °C
|
Solid properties
|
Std enthalpy change of formation, ΔfHosolid
| ? kJ/mol
|
Standard molar entropy, Sosolid
| ? J/(mol K)
|
Heat capacity, cp
| ? J/(mol K)
|
Liquid properties
|
Std enthalpy change of formation, ΔfHoliquid
| ? kJ/mol
|
Standard molar entropy, Soliquid
| ? J/(mol K)
|
Heat capacity, cp
| 80.80 J/(mol K)
|
Gas properties
|
Std enthalpy change of formation, ΔfHogas
| −45.92 kJ/mol
|
Standard molar entropy, Sogas
| 192.77 J/(mol K)
|
Heat capacity, cp
| 35.06 J/(mol K)
|
Heat capacity ratio, γ at 15°C
| 1.310
|
Vapor-Liquid Equilibrium Data
P in mm Hg | 1 | 10 | 40 | 100 | 400 | 760 | 1520 | 3800 | 7600 | 15600 | 30400 | 45600
|
T in °C | –109.1(s) | –91.9(s) | –79.2(s) | –68.4 | –45.4 | –33.6 | –18.7 | 4.7 | 25.7 | 50.1 | 78.9 | 98.3
|
Table data (above) obtained from CRC Handbook of Chemistry and Physics 44th ed. The (s) notation indicates equilibrium temperature of vapor over solid. Otherwise temperature is equilibrium of vapor over liquid.
Vapor pressure formula for ammonia:[1]
- log10(P) = A – B / (T – C)
where P is pressure in kPa and T is temperature in Kelvins
- A = 6.67956; B = 1002.711; C = 25.215 for T = 190 K through 333 K
-
Vapor over Anhydrous Ammonia[2]
|
Temp.
| Pressure
| ρ of liquid
| ρ of vapor
| ΔvapH
|
–78 °C | 5.90 kPa
| |
|
–75 °C | 7.93 kPa
| 0.73094 g/cm3
| 7.8241×10–5 g/cm3
|
|
–70 °C | 10.92 kPa
| 0.72527 g/cm3
| 1.1141×10–4 g/cm3
|
|
–65 °C | 15.61 kPa
| 0.71953 g/cm3
| 1.5552×10–4 g/cm3
|
|
–60 °C | 21.90 kPa
| 0.71378 g/cm3
| 2.1321×10–4 g/cm3
|
|
–55 °C | 30.16 kPa
| 0.70791 g/cm3
| 2.8596×10–4 g/cm3
|
|
–50 °C | 40.87 kPa
| 0.70200 g/cm3
| 3.8158×10–4 g/cm3
| 1417 J/g
|
–45 °C | 54.54 kPa
| 0.69604 g/cm3
| 4.9940×10–4 g/cm3
| 1404 J/g
|
–40 °C | 71.77 kPa
| 0.68999 g/cm3
| 6.4508×10–4 g/cm3
| 1390 J/g
|
–35 °C | 93.19 kPa
| 0.68385 g/cm3
| 8.2318×10–4 g/cm3
| 1375 J/g
|
–30 °C | 119.6 kPa
| 0.67764 g/cm3
| 1.0386×10–3 g/cm3
| 1361 J/g
|
–25 °C | 151.6 kPa
| 0.67137 g/cm3
| 1.2969×10–3 g/cm3
| 1345 J/g
|
–20 °C | 190.2 kPa
| 0.66503 g/cm3
| 1.6039×10–3 g/cm3
| 1330 J/g
|
–15 °C | 236.3 kPa
| 0.65854 g/cm3
| 1.9659×10–3 g/cm3
| 1314 J/g
|
–10 °C | 290.8 kPa
| 0.65198 g/cm3
| 2.3874×10–3 g/cm3
| 1297 J/g
|
–5 °C | 354.8 kPa
| 0.64533 g/cm3
| 2.8827×10–3 g/cm3
| 1280 J/g
|
0 °C | 429.4 kPa
| 0.63857 g/cm3
| 3.4528×10–3 g/cm3
| 1263 J/g
|
5 °C | 515.7 kPa
| 0.63167 g/cm3
| 4.1086×10–3 g/cm3
| 1245 J/g
|
10 °C | 614.9 kPa
| 0.62469 g/cm3
| 4.8593×10–3 g/cm3
| 1226 J/g
|
15 °C | 728.3 kPa
| 0.61755 g/cm3
| 5.7153×10–3 g/cm3
| 1207 J/g
|
20 °C | 857.1 kPa
| 0.61028 g/cm3
| 6.6876×10–3 g/cm3
| 1187 J/g
|
25 °C | 1003 kPa
| 0.60285 g/cm3
| 7.7882×10–3 g/cm3
| 1167 J/g
|
30 °C | 1166 kPa
| 0.59524 g/cm3
| 9.0310×10–3 g/cm3
| 1146 J/g
|
35 °C | 1350 kPa
| 0.58816 g/cm3
| 1.0431×10–2 g/cm3
| 1124 J/g
|
40 °C | 1554 kPa
| 0.57948 g/cm3
| 1.2006×10–2 g/cm3
| 1101 J/g
|
45 °C | 1781 kPa
| 0.57130 g/cm3
| 1.3775×10–2 g/cm3
| 1083 J/g
|
50 °C | 2032 kPa
| 0.56287 g/cm3
| 1.5761×10–2 g/cm3
| 1052 J/g
|
55 °C | 2310 kPa
| 0.55420 g/cm3 |
|
|
60 °C | 2613 kPa
| 0.54523 g/cm3
| 2.05×10–2 g/cm3
|
|
65 °C | 2947 kPa
| 0.53596 g/cm3 |
|
|
70 °C | 3312 kPa
| 0.52632 g/cm3
| 2.65×10–2 g/cm3
|
|
75 °C | 3711 kPa
| 0.51626 g/cm3 |
|
|
80 °C | 4144 kPa
| 0.50571 g/cm3
| 3.41×10–2 g/cm3
|
|
85 °C | 4614 kPa
| 0.49463 g/cm3 |
|
|
90 °C | 5123 kPa
| 0.48290 g/cm3
| 4.39×10–2 g/cm3
|
|
95 °C | 5672 kPa
| 0.47041 g/cm3 |
|
|
100 °C | 6264 kPa
| 0.45693 g/cm3
| 5.68×10–2 g/cm3
|
|
Temp.
| Pressure
| ρ of liquid
| ρ of vapor
| ΔvapH
|
The table above gives properties of the vapor-liquid equilibrium of anhydrous ammonia at various temperatures. The second column is vapor pressure in kPa. The third column is the density of the liquid phase. The fourth column is the density of the vapor. The fifth column is the heat of vaporization needed to convert one gram of liquid to vapor.
|
| |
Vapor over Aqueous Ammonia Solution[3]
|
Temp.
| %wt NH3
| Partial Pressure NH3
| Partial Pressure H2O
|
0 °C | 4.72 | 1.52 kPa
| 0.68 kPa
|
9.15 | 3.31 kPa | 0.71 kPa
|
14.73 | 6.84 kPa | 0.55 kPa
|
19.62 | 11.0 kPa | 0.40 kPa
|
22.90 | 14.9 kPa | 0.37 kPa
|
10 °C | 4.16 | 2.20 kPa
| 1.21 kPa
|
8.26 | 4.96 kPa | 1.17 kPa
|
12.32 | 8.56 kPa | 1.01 kPa
|
15.88 | 12.68 kPa
| 0.93 kPa
|
20.54 | 19.89 kPa
| 0.83 kPa
|
21.83 | 22.64 kPa
| 0.73 kPa
|
19.9 °C | 4.18 | 3.65 kPa
| 2.19 kPa
|
6.50 | 6.11 kPa | 2.15 kPa
|
6.55 | 6.13 kPa | 2.13 kPa
|
7.72 | 7.49 kPa | 2.08 kPa
|
10.15 | 10.75 kPa
| 2.01 kPa
|
10.75 | 11.51 kPa
| 1.96 kPa
|
16.64 | 22.14 kPa
| 1.72 kPa
|
19.40 | 28.74 kPa
| 1.64 kPa
|
23.37 | 40.32 kPa
| 1.37 kPa
|
30.09 °C | 3.93 | 5.49 kPa
| 4.15 kPa
|
7.43 | 11.51 kPa | 3.89 kPa
|
9.75 | 16.00 kPa | 3.80 kPa
|
12.77 | 23.33 kPa
| 3.55 kPa
|
17.76 | 38.69 kPa
| 3.31 kPa
|
17.84 | 38.81 kPa
| 3.24 kPa
|
21.47 | 53.94 kPa
| 2.95 kPa
|
40 °C | 3.79 | 8.15 kPa
| 7.13 kPa
|
7.36 | 17.73 kPa | 6.76 kPa
|
11.06 | 29.13 kPa
| 6.55 kPa
|
15.55 | 47.14 kPa
| 5.52 kPa
|
17.33 | 57.02 kPa
|
|
20.85 | 76.81 kPa
| 5.04 kPa
|
50 °C | 3.29 | 10.54 kPa
| 11.95 kPa
|
5.90 | 20.17 kPa | 11.61 kPa
|
8.91 | 32.88 kPa | 11.07 kPa
|
11.57 | 45.56 kPa
| 10.75 kPa
|
14.15 | 60.18 kPa
| 10.27 kPa
|
14.94 | 64.94 kPa
| 10.03 kPa
|
60 °C | 3.86 | 18.25 kPa
| 19.21 kPa
|
5.77 | 28.78 kPa |
|
7.78 | 40.05 kPa | 18.47 kPa
|
9.37 | 50.09 kPa | 18.07 kPa
|
9.37 | 63.43 kPa | 17.39 kPa
|
Temp.
| %wt NH3
| Partial Pressure NH3
| Partial Pressure H2O
|
|
Heat capacity of liquid and vapor
Spectral data
UV-Vis
|
λmax
| None nm
|
Extinction coefficient, ε
| None
|
IR
|
Major absorption bands
| 3444, 3337, 1627, 950 cm−1
|
NMR
|
Proton NMR
|
|
Carbon-13 NMR
| None - no carbons
|
Other NMR data
|
|
MS
|
Masses of main fragments
| 17 (100%) 16(80%) 15(9%)
|
Regulatory data
Material Safety Data Sheet
The handling of this chemical may incur notable safety precautions. It is highly recommend that you seek the Material Safety Datasheet (MSDS) for this chemical from a reliable source such as SIRI, and follow its directions.
References
- ^ Lange's Handbook of Chemistry, 10th ed. page 1436
- ^ Lange's Handbook of Chemistry, 10th ed. page 1451 and 1468
- ^ Perman, Jour. Chem. Soc. 83 1168 (1903)
- ^ a b Pure Components Properties (Queriable database). Chemical Engineering Research Information Center. Retrieved on 1 June 2007.
Except where noted otherwise, data relate to standard ambient temperature and pressure.
Disclaimer applies.