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authorpriyanka2015-06-24 15:03:17 +0530
committerpriyanka2015-06-24 15:03:17 +0530
commitb1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (patch)
treeab291cffc65280e58ac82470ba63fbcca7805165 /858/CH9
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initial commit / add all books
Diffstat (limited to '858/CH9')
-rwxr-xr-x858/CH9/EX9.1/example_1.sce30
-rwxr-xr-x858/CH9/EX9.2/example_2.sce36
-rwxr-xr-x858/CH9/EX9.3/example_3.sce38
-rwxr-xr-x858/CH9/EX9.4/example_4.sce5
-rwxr-xr-x858/CH9/EX9.5/example_5.sce5
-rwxr-xr-x858/CH9/EX9.6/example_6.sce5
6 files changed, 119 insertions, 0 deletions
diff --git a/858/CH9/EX9.1/example_1.sce b/858/CH9/EX9.1/example_1.sce
new file mode 100755
index 000000000..426bced1c
--- /dev/null
+++ b/858/CH9/EX9.1/example_1.sce
@@ -0,0 +1,30 @@
+clc
+clear
+printf("example 9.1 page number 384\n\n")
+
+//to find the pressure drop in the coil
+
+D = 38*10^-3; //in m
+U = 1 //in m/s
+density = 998 //in kg/cubic m
+viscosity = 8*10^-4 //in Pa-s
+DC = 1 //in m
+N = 10
+e = 4*10^-6; //in m
+
+Re = (density*U*D)/viscosity;
+printf ("Reynolds number = %f",Re)
+
+f = (4*log10((e/D)/3.7+(6.81/Re)^0.9))^-2;
+printf("\n\nfriction factor = %f",f);
+
+L = 3.14*DC*N;
+
+delta_Pstr = (2*f*U*density*L)/D;
+printf("\n\npressure drop through straight pipe = %f Pa",delta_Pstr)
+
+S = 1+3.54*(D/DC);
+printf("\n\ncorrection factor = %f",S)
+
+delta_P = S*delta_Pstr
+printf("\n\npressure drop of coil = %f Pa",delta_P)
diff --git a/858/CH9/EX9.2/example_2.sce b/858/CH9/EX9.2/example_2.sce
new file mode 100755
index 000000000..44c396fc5
--- /dev/null
+++ b/858/CH9/EX9.2/example_2.sce
@@ -0,0 +1,36 @@
+clc
+clear
+printf("example 9.2 page number 384\n\n")
+
+//to find the shell side pressure drop in heat exchanger
+
+U = 0.5 //in m/s
+N = 19;
+DT = 0.026 //in m
+L = 2.7 //in m
+DS = 0.2 //in m
+e = 0.0002 //in m
+density = 836 //in kg/cu m
+viscosity = 0.00032 //in Pa s
+Pr = 6.5;
+Prw = 7.6;
+
+
+HYDIA = (DS^2-N*DT^2)/(DS+N*DT);
+
+Re = HYDIA*U*density/viscosity;
+printf ("Reynolds number = %f",Re)
+
+f = (4*log10((e/HYDIA)/3.7+(6.81/Re)^0.9))^-2;
+printf("\n\nfriction factor = %f",f);
+
+L = 3.14*DT*N;
+
+delta_Pstr = (2*f*U*density*L)/HYDIA;
+printf("\n\npressure drop through straight pipe = %f Pa",delta_Pstr)
+
+S = (Prw/Pr)^0.33;
+printf("\n\ncorrection factor = %f",S)
+
+delta_P = S*delta_Pstr
+printf("\n\npressure drop of coil = %f Pa",delta_P)
diff --git a/858/CH9/EX9.3/example_3.sce b/858/CH9/EX9.3/example_3.sce
new file mode 100755
index 000000000..666e30261
--- /dev/null
+++ b/858/CH9/EX9.3/example_3.sce
@@ -0,0 +1,38 @@
+clc
+clear
+printf("example 9.3 page number 385\n\n")
+
+MH = 10 //in kg/s
+MC = 12.5 //in kg/s
+CPH = 4.2 //in kJ/kg
+CPC = 4.2 //in kJ/kg
+THI = 353 //in K
+THO = 333 //in K
+TCI = 300 //in K
+U = 1.8 //in kW/sq m K
+
+Q = MH*CPH*(THI-THO);
+printf("heat load = %f J",Q)
+
+TCO = Q/(MC*CPC)+TCI;
+printf("\n\ncold fluid outlet temperature = %f K",TCO)
+
+//for co current flow
+
+DT1 = THI-TCO;
+DT2 = THO-TCO;
+
+LMTD = (DT1-DT2)/log(DT1/DT2);
+
+A = Q/(U*LMTD);
+printf("\n\nfor co current flow, area = %f sq m",A);
+
+//for counter current flow
+
+DT1 = THI-TCO;
+DT2 = THO-TCI;
+
+LMTD = (DT1-DT2)/log(DT1/DT2);
+
+A = Q/(U*LMTD);
+printf("\n\nfor counter current flow, area = %f sq m",A);
diff --git a/858/CH9/EX9.4/example_4.sce b/858/CH9/EX9.4/example_4.sce
new file mode 100755
index 000000000..4158067fb
--- /dev/null
+++ b/858/CH9/EX9.4/example_4.sce
@@ -0,0 +1,5 @@
+clc
+clear
+printf("example 9.4 page number 387\n\n")
+
+printf("this is a theoretical question, book shall be referred for solution")
diff --git a/858/CH9/EX9.5/example_5.sce b/858/CH9/EX9.5/example_5.sce
new file mode 100755
index 000000000..e525db72d
--- /dev/null
+++ b/858/CH9/EX9.5/example_5.sce
@@ -0,0 +1,5 @@
+clc
+clear
+printf("example 9.5 page number 392\n\n")
+
+printf("this is a theoretical question, book shall be referred for solution")
diff --git a/858/CH9/EX9.6/example_6.sce b/858/CH9/EX9.6/example_6.sce
new file mode 100755
index 000000000..4cfdf559b
--- /dev/null
+++ b/858/CH9/EX9.6/example_6.sce
@@ -0,0 +1,5 @@
+clc
+clear
+printf("example 9.6 page number 395\n\n")
+
+printf("this is a theoritical problem, book shall be referred for solution")