Ammonia is oxidized in a continuous reactor 4NH3 g + 5O2 g --> 4NO g + 6H2O g delta AHr= -904.7KJ mol The feed stream (40 mole% NH3 and 60 mole% O2 )enters the reactor at 200 degrees celsius with 80% conversion of ammonia and the products leave at 300 degrees celsius. Determine the quantity of heat required to be added or removed from the reactor.  The basis of calculation: 10mol/s of feed stream. given: the constant heat capacity, Cp, of NH3(g), O2(g), NO(g), and H2O(v) are 0.035, 0.029, 0.029 and 0.033KJ/ mol. degrees celsius respectively.) Cp O2 or table 8 for the calculation.  can you please explaing each step

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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Ammonia is oxidized in a continuous reactor 4NH3 g + 5O2 g --> 4NO g + 6H2O g delta AHr= -904.7KJ mol The feed stream (40 mole% NH3 and 60 mole% O2 )enters the reactor at 200 degrees celsius with 80% conversion of ammonia and the products leave at 300 degrees celsius. Determine the quantity of heat required to be added or removed from the reactor. 

The basis of calculation: 10mol/s of feed stream.

given: the constant heat capacity, Cp, of NH3(g), O2(g), NO(g), and H2O(v) are 0.035, 0.029, 0.029 and 0.033KJ/ mol. degrees celsius respectively.) Cp O2 or table 8 for the calculation. 

can you please explaing each step 

H(kJ/mol)
Reference state: Gas, Pref = 1 atm, Tref = 25°C
T
Air 0₂ N₂
-0.72 -0.73
-0.73
0.00 0.00 0.00
2.19 2.24 2.19
5.31 5.13
300 8.17 8.47 8.12 7.96 8.17 11.58 9.57
0
25
100
200
H₂
со CO2 H2O
-0.72 -0.73 -0.92 -0.84
0.00
0.00
2.16 2.19 2.90
5.15
500
5.06
5.16
0.00
7.08
0.00
2.54
6.01
400 11.24 11.72 11.15 10.89 11.25 16.35 13.23
14.37 15.03 14.24 13.83 14.38 21.34 17.01
600 17.55 18.41 17.39 16.81 17.57 26.53 20.91
700 20.80 21.86 20.59 19.81 20.82 31.88 24.92
800 24.10 25.35 23.86 22.85 24.13 37.36 29.05
900 27.46 28.89 27.19 25.93 27.49 42.94 33.32
1000 30.86 32.47 30.56 29.04 30.91 48.60 37.69
1100 34.31 36.07 33.99 32.19 34.37 54.33 42.18
1200 37.81 39.70 37.46 35.39 37.87 60.14 46.78
1300 41.34 43.38 40.97 38.62 41.40 65.98 51.47
1400 44.89 47.07 44.51 41.90 44.95 71.89 56.25
1500 48.45 50.77 48.06 45.22 48.51 77.84 61.09
Transcribed Image Text:H(kJ/mol) Reference state: Gas, Pref = 1 atm, Tref = 25°C T Air 0₂ N₂ -0.72 -0.73 -0.73 0.00 0.00 0.00 2.19 2.24 2.19 5.31 5.13 300 8.17 8.47 8.12 7.96 8.17 11.58 9.57 0 25 100 200 H₂ со CO2 H2O -0.72 -0.73 -0.92 -0.84 0.00 0.00 2.16 2.19 2.90 5.15 500 5.06 5.16 0.00 7.08 0.00 2.54 6.01 400 11.24 11.72 11.15 10.89 11.25 16.35 13.23 14.37 15.03 14.24 13.83 14.38 21.34 17.01 600 17.55 18.41 17.39 16.81 17.57 26.53 20.91 700 20.80 21.86 20.59 19.81 20.82 31.88 24.92 800 24.10 25.35 23.86 22.85 24.13 37.36 29.05 900 27.46 28.89 27.19 25.93 27.49 42.94 33.32 1000 30.86 32.47 30.56 29.04 30.91 48.60 37.69 1100 34.31 36.07 33.99 32.19 34.37 54.33 42.18 1200 37.81 39.70 37.46 35.39 37.87 60.14 46.78 1300 41.34 43.38 40.97 38.62 41.40 65.98 51.47 1400 44.89 47.07 44.51 41.90 44.95 71.89 56.25 1500 48.45 50.77 48.06 45.22 48.51 77.84 61.09
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