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/CH6/EX6.3/6_03.sce | 62 ++++++++++++++++++++++++++++++++++++++++++++++++++
 1 file changed, 62 insertions(+)
 create mode 100755 249/CH6/EX6.3/6_03.sce

(limited to '249/CH6/EX6.3')

diff --git a/249/CH6/EX6.3/6_03.sce b/249/CH6/EX6.3/6_03.sce
new file mode 100755
index 000000000..b938d3502
--- /dev/null
+++ b/249/CH6/EX6.3/6_03.sce
@@ -0,0 +1,62 @@
+clear
+clc
+CAo=[2;5;6;6;11;14;16;24];//mmol/m3
+CA=[0.5;3;1;2;6;10;8;4];//mmol/m3
+t=[30;1;50;8;4;20;20;4];//min
+vo=0.1;//m3/min
+for i=1:8
+    inv_rA(i)=t(i)/(CAo(i)-CA(i));
+end
+//Sorting CA and accordingly changing -1/rA for plotting graph between CA and -1/rA
+for i=1:8
+    for j=i:8
+        if CA(i)>CA(j)
+        temp=CA(i);
+        CA(i)=CA(j);
+        CA(j)=temp;
+        temp1=inv_rA(i);
+        inv_rA(i)=inv_rA(j);
+        inv_rA(j)=temp1;
+        end
+    end
+end
+plot(CA,inv_rA)
+xlabel('CA(mmol/m3)');ylabel('-1/rA(m3.min/m mol)');
+disp('From the graph,we can see that we should use plug flow with recycle')
+//From fig
+CAin=6.6;//mmol/m3
+R=(10-6.6)/(6.6-1);
+//V=t*vo=area*vo
+V=(10-1)*1.2*vo;
+vr=vo*R;
+printf("\n Part a")
+printf("\n  The vol of reactor is %f",V)
+printf("m3 \n The recycle flow rate is %f",vr)
+printf("m3/min")
+//Part b,from fig
+t=(10-1)*10;
+t1=(10-2.6)*0.8;
+t2=(2.6-1)*10;
+//For 1  tank
+V=t*vo;
+//For  2 tank
+V1=t1*vo;
+V2=t2*vo;
+Vt=V1+V2;
+printf("\n Part b")
+printf("\n For 1 tank volume is %f",V)
+printf("m3 \n For 2 tank the volume is %f",Vt)
+printf("m3")
+printf("\n Part c")
+disp('We should use mixed flow followed by plug flow')
+//For MFR
+tm=(10-4)*0.2;
+Vm=tm*vo;
+//For PFR
+tp=5.8;//by graphical integration
+Vp=tp*vo;
+Vtotal=Vp+Vm;
+printf("\n For MFR volume(m3) is %f",Vm)
+printf("\n For PFR volume(m3) is %f",Vp)
+printf("\n Total volume is %f",Vtotal)
+printf("m3")
\ No newline at end of file
-- 
cgit