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/CH5/EX5.1/5_01.sce | 25 +++++++++++++++++++++++++
 249/CH5/EX5.2/5_02.sce | 37 +++++++++++++++++++++++++++++++++++++
 249/CH5/EX5.3/5_03.sce | 18 ++++++++++++++++++
 249/CH5/EX5.4/5_04.sce | 14 ++++++++++++++
 249/CH5/EX5.5/5_05.sce | 17 +++++++++++++++++
 249/CH5/EX5.6/5_06.sce |  4 ++++
 6 files changed, 115 insertions(+)
 create mode 100755 249/CH5/EX5.1/5_01.sce
 create mode 100755 249/CH5/EX5.2/5_02.sce
 create mode 100755 249/CH5/EX5.3/5_03.sce
 create mode 100755 249/CH5/EX5.4/5_04.sce
 create mode 100755 249/CH5/EX5.5/5_05.sce
 create mode 100755 249/CH5/EX5.6/5_06.sce

(limited to '249/CH5')

diff --git a/249/CH5/EX5.1/5_01.sce b/249/CH5/EX5.1/5_01.sce
new file mode 100755
index 000000000..2a11a606b
--- /dev/null
+++ b/249/CH5/EX5.1/5_01.sce
@@ -0,0 +1,25 @@
+clear
+clc
+//Given
+//Concentrations in mol/litre
+CAo=0.1;CBo=0.01;Cco=0;CAf=0.02;CBf=0.03;Ccf=0.04;
+//Volume in litre
+V=1;
+//Volumetric flow rate(l/min)
+v=1;
+//For mixed flow reactor
+CA=CAf;CB=CBf;Cc=Ccf;
+//Rate of reaction(mol/litre.min)
+rA=(CAo-CA)/(V/v);
+rB=(CBo-CB)/(V/v);
+rc=(Cco-Cc)/(V/v);
+printf("\nRESULT\n")
+printf("rate of reaction of A(mol/litre.min) is %f\n",rA)
+printf("\nrate of reaction of B(mol/litre.min) is %f\n",rB)
+printf("\nrate of reaction of C(mol/litre.min) is %f\n",rc)
+
+
+
+
+
+
diff --git a/249/CH5/EX5.2/5_02.sce b/249/CH5/EX5.2/5_02.sce
new file mode 100755
index 000000000..0f9eb6da2
--- /dev/null
+++ b/249/CH5/EX5.2/5_02.sce
@@ -0,0 +1,37 @@
+clear
+clc
+//Given
+//Volumetric flow rates(litre/hr)
+vo=[10;3;1.2;0.5];
+//Concentrations (millimol/litre)
+CA=[85.7;66.7;50;33.4];
+CAo=100;
+//Volume(litre)
+V=0.1;
+//For the stoichiometry 2A-->R
+//Expansion factor is
+e=(1-2)/2;
+//Initialization
+XA=zeros(4,1);
+rA=zeros(4,1);
+//Relation between concentration and conversion
+for i=1:4
+XA(i)=(1-CA(i)/CAo)/(1+e*CA(i)/CAo);
+//Rate of reaction is given by
+rA(i)=vo(i)*CAo*XA(i)/V;
+//Testing nth order kinetics
+//-rA=k*CA^n
+//log(-rA)=logk+nlog(CA)
+m(i)=log10(CA(i));
+n(i)=log10(rA(i));
+end
+//For nth order plot between n & m should give a straight line
+plot(m,n)
+coefs=regress(m,n);
+printf("Intercept of the graph is %f\n",coefs(1))
+printf("Slope of the graph is %f\n",coefs(2))
+k=10^coefs(1)
+n=coefs(2)
+printf("\n Taking n=2,rate of equation(millimol/litre.hr) is %f",k)
+printf("CA^2 \n")
+disp('The sol slightly differ from that given in book because regress fn is used to calculate the slope')
\ No newline at end of file
diff --git a/249/CH5/EX5.3/5_03.sce b/249/CH5/EX5.3/5_03.sce
new file mode 100755
index 000000000..d2c67d8a7
--- /dev/null
+++ b/249/CH5/EX5.3/5_03.sce
@@ -0,0 +1,18 @@
+clear
+clc
+//Concentration(mol/litre) of components in the mixed feed stream is
+CAo=1.4;CBo=0.8;CRo=0;
+//Volume(litre)
+V=6;
+//For 75% conversion of B
+//From stoichiometry of equation A+2B-->R
+CA=1.4-(0.75*0.8)/2;
+CB=0.8-(0.75*0.8);
+CR=(0.75*0.8)/2;
+//From the Given rate equation(mol/litre.min)
+rB=2*(12.5*CA*CB*CB-1.5*CR);
+//Volumetric flow rate is given by
+v=V*rB/(CBo-CB);
+printf("\n volumetric flow rate(litre/min) into and out of the reactor is %f \n",v)
+disp('The sol varies from book as the value of CB taken in book at end is wrong')
+
diff --git a/249/CH5/EX5.4/5_04.sce b/249/CH5/EX5.4/5_04.sce
new file mode 100755
index 000000000..dda8acc7c
--- /dev/null
+++ b/249/CH5/EX5.4/5_04.sce
@@ -0,0 +1,14 @@
+clear
+clc
+//With 50% inert 2 vol of feed would give 4 vol of completely converted gas
+//Expansion factor is
+eA=(4-2)/2;
+//Initial concentration of A(mol/litre)
+CAo=0.0625;
+//For 80% conversion
+xAo=0;xAf=0.8;k=0.01;
+//For plug flow space time(t) is given by
+//t=CAo*integral(dxA/-rA)
+X=integrate('sqrt((1+xA)/(1-xA))','xA',xAo,xAf);
+t=sqrt(CAo)*X/k;
+printf("\n Space time(sec) needed is %f \n",t)
\ No newline at end of file
diff --git a/249/CH5/EX5.5/5_05.sce b/249/CH5/EX5.5/5_05.sce
new file mode 100755
index 000000000..dc73a5216
--- /dev/null
+++ b/249/CH5/EX5.5/5_05.sce
@@ -0,0 +1,17 @@
+clear
+clc
+//Given
+//Temperature(kelvin)
+T=922;
+//Pressure(Pascal)
+P=460000;
+//Let A=PH3,R=P4,S=H2
+FAo=40;//mol/hr
+k=10;//(/hr)
+R=8.314;
+CAo=P/(R*T);// mol/m3
+e=(7-4)/4;
+XA=0.8;
+//The volume of plug flow reactor is given by
+V=FAo*[(1+e)*log(1/(1-XA))-e*XA]/(k*CAo);
+printf("\n volume(m3) of reactor is %f \n",V)
\ No newline at end of file
diff --git a/249/CH5/EX5.6/5_06.sce b/249/CH5/EX5.6/5_06.sce
new file mode 100755
index 000000000..2a35eb2ee
--- /dev/null
+++ b/249/CH5/EX5.6/5_06.sce
@@ -0,0 +1,4 @@
+clear
+clc
+//This is a theorotical Qn
+printf("Its a theorotical Question")
\ No newline at end of file
-- 
cgit