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