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diff --git a/1040/CH3/EX3.7/Chapter3_Ex7_Output.txt b/1040/CH3/EX3.7/Chapter3_Ex7_Output.txt new file mode 100644 index 000000000..cbe7963ea --- /dev/null +++ b/1040/CH3/EX3.7/Chapter3_Ex7_Output.txt @@ -0,0 +1,30 @@ +
+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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