From b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b Mon Sep 17 00:00:00 2001
From: priyanka
Date: Wed, 24 Jun 2015 15:03:17 +0530
Subject: initial commit / add all books

---
 249/CH7/EX7.3/7_03.sce | 28 ++++++++++++++++++++++++++++
 1 file changed, 28 insertions(+)
 create mode 100755 249/CH7/EX7.3/7_03.sce

(limited to '249/CH7/EX7.3')

diff --git a/249/CH7/EX7.3/7_03.sce b/249/CH7/EX7.3/7_03.sce
new file mode 100755
index 000000000..b404c196e
--- /dev/null
+++ b/249/CH7/EX7.3/7_03.sce
@@ -0,0 +1,28 @@
+clear
+clc
+CAo=2;
+//Since S is the desired Product
+//Q(S/A)=2CA/(1+CA)^2
+//Part a
+//Csf=(CAo-CA)*2*CA/(1+CA)^2
+//on differentiating this to get max Csf,we get max value at
+CA=0.5;
+Csf=(CAo-CA)*2*CA/(1+CA)^2;
+printf("\n Part a")
+printf("\n For Mixed Flow Reactor")
+printf("\n Maximum expected Cs is %f",Csf)
+//For Plug Flow Reactor
+//Production of s is max at 100% Conversion of A
+CAf=0;
+Csf=-1*integrate('2*CA/(1+CA)^2','CA',CAo,CAf);
+printf("\n Part b")
+printf("\n For Plug Flow")
+printf("\n Maximum expected concentration of S is %f \n",Csf)
+//Part C
+//Since no reactant leaves the system unconverted,what is important is to operate at condition of highest fractional yield
+//ie. at CA=1 where Q(S/A)=0.5
+CA=1;
+Csf=(CAo-CA)*2*CA/(1+CA)^2;
+printf("Part c")
+printf("\n For MFR with separation and recycle" )
+printf("\n Concentration of Csf is %f",Csf)
\ No newline at end of file
-- 
cgit