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authorprashantsinalkar2017-10-10 12:27:19 +0530
committerprashantsinalkar2017-10-10 12:27:19 +0530
commit7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch)
treedbb9e3ddb5fc829e7c5c7e6be99b2c4ba356132c /965/CH3
parentb1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff)
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Diffstat (limited to '965/CH3')
-rw-r--r--965/CH3/EX3.1/1.sci40
-rw-r--r--965/CH3/EX3.3/3.sci12
-rw-r--r--965/CH3/EX3.4/4.sci14
-rw-r--r--965/CH3/EX3.5/5.sci18
-rw-r--r--965/CH3/EX3.6/6.sci16
-rw-r--r--965/CH3/EX3.7/7.sci19
-rw-r--r--965/CH3/EX3.8/8.sci22
7 files changed, 141 insertions, 0 deletions
diff --git a/965/CH3/EX3.1/1.sci b/965/CH3/EX3.1/1.sci
new file mode 100644
index 000000000..5518f928a
--- /dev/null
+++ b/965/CH3/EX3.1/1.sci
@@ -0,0 +1,40 @@
+clc;
+clear all;
+disp("steady state temperature distribution")
+disp("Let th = t-ta")
+disp("the controllign differential equation for the given problem is given by")
+disp("d2th/dx2+d2th/dy2 =0------(1)")
+disp("the boundary conditions are :")
+disp("i) at x = infinity, th =0")
+disp("ii) at x = 0, th =th0")
+disp("iii) at y =L, th =0")
+disp("iv) at y = 0, th =0")
+disp("The solution of eq. 1 is th = X(x)Y(y) ------ (2)")
+disp("substituting the solution in controlling equation, we get ")
+disp("1/X*d2X/dx2 =-1/Y*d2Y/dy2 = + or - lambda^2")
+disp("The required equations are :")
+disp("d2X^2/dx2-lambda^2*X =0 ------(iii)")
+disp("d2Y^2/dy2+lambda^2*Y =0 ------(iv)")
+disp("the solutions of eqns are :")
+disp("X = A*exp(lambda*x)+B*exp(-lambda*x)")
+disp("Y = C*cos(lambda*y)+D*sin(lambda*y)")
+disp("th = (A*exp(lambda*x)+B*exp(-lambda*x))*(C*cos(lambda*y)+D*sin(lambda*y))")
+disp(" from boundary condition i), we have ")
+disp("0 = (A*exp(lambda*x)+B*exp(-lambda*x))*(C*cos(lambda*y)+D*sin(lambda*y)")
+disp("A = 0 and th =B*(C*cos(lambda*y)+D*sin(lambda*y)")
+disp("from boundary condition iv), we have")
+disp("0 = C*B*exp(-lambda*x)")
+disp("hence C = 0 and equation reduces to th = B*D*sin(lambda*y)*exp(-lambda*x)")
+disp("from boundary condition iii) we get, 0 = E*exp(-lambda*x)*sin(lambda*L), where E = B*D")
+disp("since E is not 0, sin (lambda*L)=0")
+disp("lambda = 0, %pi/L,2*%pi/L.....")
+disp("lambdan = n*%pi/L, where n = 0,1,2....")
+disp("hence , th = E*exp(-lambdan*x)*sin(lambdan*y)")
+disp("from boundary eqn ii) we have ")
+disp("th = sum(En*sin(lambdan*y), 1, infinity)")
+disp("This is an expression of th0 in terms of Fourier series, where En are Fourier coefficients.")
+disp("by integrating we get")
+disp("th = 2*th0/L*(sum(((1-(-1)^n)/lambdan *exp(-lambdan*x)*sin(lambdan*y))")
+
+,
+
diff --git a/965/CH3/EX3.3/3.sci b/965/CH3/EX3.3/3.sci
new file mode 100644
index 000000000..f5ec0484a
--- /dev/null
+++ b/965/CH3/EX3.3/3.sci
@@ -0,0 +1,12 @@
+clc;
+clear all;
+disp("Heat loss calculation")
+r=0.6/2;//m
+L=1;//m
+H=1.8;//m
+k=0.51;// W/(m*C)
+tp=95;// degree C
+te=25;// degree C
+Sfc=2*3.1416*L/(log(2*H/r));
+Q=k*Sfc*(tp-te);
+disp("W",Q,"Heat loss from the pipe meter length, Q =")
diff --git a/965/CH3/EX3.4/4.sci b/965/CH3/EX3.4/4.sci
new file mode 100644
index 000000000..545ca9a36
--- /dev/null
+++ b/965/CH3/EX3.4/4.sci
@@ -0,0 +1,14 @@
+clc;
+clear all;
+disp("Sphere Surface temperature")
+r=1.6/2;//m
+
+H=5.5;//m
+k=0.51;// W/(m*C)
+Qg=580;// W
+
+te=6;// degree C
+Sfc=4*3.1416*r/(1-r/(2*H));
+//Qg=k*Sfc*(t-te);
+t=Qg/(k*Sfc)+te;
+disp("degree C",t,"surface temperature of sphere, t =")
diff --git a/965/CH3/EX3.5/5.sci b/965/CH3/EX3.5/5.sci
new file mode 100644
index 000000000..52758e6cf
--- /dev/null
+++ b/965/CH3/EX3.5/5.sci
@@ -0,0 +1,18 @@
+clc;
+clear all;
+disp("Heat loss/length")
+a=0.6;// m
+b=0.45;//m
+H=1.5;//m
+k=0.51;// W/(m*C)
+tp=105;// degree C
+ts=5;// degree C
+
+x=log(1+H/a);
+y=H/b;
+
+Sfc=2.756*((x^(-.59))*(y^(-.078)));
+
+Q=k*Sfc*(tp-ts);
+
+disp("W",Q,"Heat loss per meter length, Q =")
diff --git a/965/CH3/EX3.6/6.sci b/965/CH3/EX3.6/6.sci
new file mode 100644
index 000000000..b95cbc9e2
--- /dev/null
+++ b/965/CH3/EX3.6/6.sci
@@ -0,0 +1,16 @@
+clc;
+clear all;
+disp("heat transfer rate, temperature")
+r1=0.600/2;// m
+r2=0.18/2;//m
+D=1.8;//m
+L=90;//m
+tp1=180;// degree C
+tp2=12;// degree C
+k=0.45;// W/(m*C)
+
+Sfc=2*3.1416*L/(acosh((D^2-r1^2-r2^2)/(2*r1*r2)));
+Sfc
+Q=k*Sfc*(tp1-tp2);
+
+disp("W",Q,"Heat loss per meter length, Q =")
diff --git a/965/CH3/EX3.7/7.sci b/965/CH3/EX3.7/7.sci
new file mode 100644
index 000000000..2332ec997
--- /dev/null
+++ b/965/CH3/EX3.7/7.sci
@@ -0,0 +1,19 @@
+clc;
+clear all;
+disp("Heat loss calculations")
+k=1.05;// W/(m*C)
+ti=600;//degree C
+to=70;// degree C
+L=0.12;//m
+A=0.6*0.6;//m^2
+Sfcwall=A/L;
+
+D=0.6;//m
+Sfcedge=0.54*D;
+
+Sfccorner=0.15*L;
+Sfct=6*Sfcwall+12*Sfcedge+8*Sfccorner;
+
+Q=k*Sfct*(ti-to);
+
+disp("W",Q,"Heat loss through walls, Q =")
diff --git a/965/CH3/EX3.8/8.sci b/965/CH3/EX3.8/8.sci
new file mode 100644
index 000000000..839c75bee
--- /dev/null
+++ b/965/CH3/EX3.8/8.sci
@@ -0,0 +1,22 @@
+clc;
+clear all;
+disp("Heat loss rate")
+ti=350;// degree C
+to=50;// degree C
+k=1.5;// W/(m*C)
+x=0.3;// m
+l=4.5;//m
+b=3.75;//m
+h=3;//m
+Ai=2*(l*b+l*h+b*h);//m^2
+y=4*(l+b+h);// length of edges
+Sfce=y;
+Sfcc=0.15*x;
+
+Am=Ai+Sfce*.54*x+8*Sfcc*x;
+Am
+disp("m^2")
+Q=k*Am*(ti-to)/x;
+disp("W",Q,"rate of heat loss Q =")
+
+