A.3-22 Equilibrium Data for Ammonia-Water SystemPartial Pressure of NH3in Vapor, p (mm Hg)Mole FractionNH, in Liquid, x₁00.01260.01670.02080.02580.03090.04050.05030.07370.09600.1370.1750.2100.2410.29720°C (293 K)0121518.224.931.750.069.611416622729847030°C (303 K)011.515.319.324.429.640.151.079.7110179260352454719Mole Fraction NH, inVapor, y; P = 1 Atm20°C00.01580.01970.02390.03280.04160.06570.09150.1500.2180.2980.3920.61830°C00.01510.02010.02540.03210.03900.05270.06710.1050.1450.2350.3420.4630.5970.945 Absorption of Ammonia in a Tray Tower. A tray tower is to be used to remove99% of the ammonia from an entering air stream containing 6 mol % ammoniaat 293 K and 1.013 × 105 Pa. The entering pure water flow rate is 188 kgH₂O/h·m² and the inert air flow is 128 kg air/h- m². Calculate the number oftheoretical trays needed. Use equilibrium data from Appendix A.3. For thedilute end of the tower, plot an expanded diagram to step off the number oftrays more accurately.

To find: The number of theoretical trays needed. Given: The liquid flow rate, L = 188 kg H2O/h.m2.…

Absorption of Ammonia in a Tray Tower. A tray tower is to be used to remove 99% of the ammonia from an entering air stream containing 6 mol % ammonia at 293 K and 1.013 x 105 Pa. The entering pure water flow rate is 188 kg H₂O/h m² and the inert air flow is 128 kg air/h m². Calculate the number of theoretical trays needed. Use equilibrium data from Appendix A.3. For the dilute end of the tower, plot an expanded diagram to step off the number of trays more accurately.

Absorption of Ammonia in a Tray Tower. A tray tower is to be used to remove 99% of the ammonia from an entering air stream containing 6 mol % ammonia at 293 K and 1.013 x 105 Pa. The entering pure water flow rate is 188 kg H₂O/h m² and the inert air flow is 128 kg air/h m². Calculate the number of theoretical trays needed. Use equilibrium data from Appendix A.3. For the dilute end of the tower, plot an expanded diagram to step off the number of trays more accurately.

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

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Question

A.3-22 Equilibrium Data for Ammonia-Water System
Partial Pressure of NH3
in Vapor, p (mm Hg)
Mole Fraction
NH, in Liquid, x₁
0
0.0126
0.0167
0.0208
0.0258
0.0309
0.0405
0.0503
0.0737
0.0960
0.137
0.175
0.210
0.241
0.297
20°C (293 K)
0
12
15
18.2
24.9
31.7
50.0
69.6
114
166
227
298
470
30°C (303 K)
0
11.5
15.3
19.3
24.4
29.6
40.1
51.0
79.7
110
179
260
352
454
719
Mole Fraction NH, in
Vapor, y; P = 1 Atm
20°C
0
0.0158
0.0197
0.0239
0.0328
0.0416
0.0657
0.0915
0.150
0.218
0.298
0.392
0.618
30°C
0
0.0151
0.0201
0.0254
0.0321
0.0390
0.0527
0.0671
0.105
0.145
0.235
0.342
0.463
0.597
0.945

Absorption of Ammonia in a Tray Tower. A tray tower is to be used to remove
99% of the ammonia from an entering air stream containing 6 mol % ammonia
at 293 K and 1.013 × 105 Pa. The entering pure water flow rate is 188 kg
H₂O/h·m² and the inert air flow is 128 kg air/h- m². Calculate the number of
theoretical trays needed. Use equilibrium data from Appendix A.3. For the
dilute end of the tower, plot an expanded diagram to step off the number of
trays more accurately.

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