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Heat Capacity evaluated at 800 K :827 (cal/°C)
Temperature Change to carry out the reaction at T_F,
using the energy to heat the product gas :210 °C
OUTPUT Ex3.7.a
============================================================================
X Phi T_eq T_eq r_max
- (atm^-0.5) (K) (°C) (gmol/g cat sec)
============================================================================
0.50 3636568.30 962 689 7.749486E-05
0.60 736637.41 927 654 5.880675E-05
0.70 171613.48 892 619 4.352732E-05
0.80 31644.93 853 580 3.044561E-05
0.90 12422.07 802 529 1.840952E-05
0.95 7367.71 760 487 1.201510E-05
OUTPUT Ex3.7.b
============================================================================
===========================================
10^-6/r X (conversion)
(gmol/g cat,s) (-)
===========================================
0.04 0.10
0.03 0.20
0.02 0.30
0.01 0.40
0.01 0.50
0.02 0.60
From graphical procedure (1/r vs x) the optimum temperature obtained is T_opt: 412°C
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