From 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 Mon Sep 17 00:00:00 2001
From: prashantsinalkar
Date: Tue, 10 Oct 2017 12:27:19 +0530
Subject: initial commit / add all books

---
 3733/CH22/EX22.1/Ex22_1.sce | 35 +++++++++++++++++++++++++++++++++++
 1 file changed, 35 insertions(+)
 create mode 100644 3733/CH22/EX22.1/Ex22_1.sce

(limited to '3733/CH22/EX22.1/Ex22_1.sce')

diff --git a/3733/CH22/EX22.1/Ex22_1.sce b/3733/CH22/EX22.1/Ex22_1.sce
new file mode 100644
index 000000000..63c5abcf8
--- /dev/null
+++ b/3733/CH22/EX22.1/Ex22_1.sce
@@ -0,0 +1,35 @@
+// Example 22_1
+clc;funcprot(0);
+//Given data
+p_1=30;// The boiler pressure in bar
+p_2=1;// The condenser pressure in bar
+
+//Calculation
+//(a)
+// From steam tables, at pressure P_b=30 bar
+h_1=2796;// kJ/kg
+//For finding the dryness-fraction of steam at the point 'c',we can equate  the entropies.
+// At pressure 30 bar=At pressure 1 bar
+// From steam tables, at pressure P_1=30 bar and P_2=1 bar
+T_s1=232.8;//°C
+T_s2=99.1;//°C
+h_f2=414.6;// kJ/kg
+h_fg1=1797;// kJ/kg
+h_fg2=2253;// kJ/kg
+v_f2=0.001043;// m^3/kg
+// Assume x_2=y(1)
+function[X]=drynessfraction(y)
+    X(1)=((2.3026*log10((T_s2+273)/273))+((y(1)*h_fg2)/(T_s2+273)))-((2.3026*log10((T_s1+273)/273))+(h_fg1/(T_s1+273)));
+endfunction
+y=[0.1];
+z=fsolve(y,drynessfraction);
+x_2=z(1);
+//x_2=z(1);// Dryness fraction
+h_2=h_f2+(x_2*h_fg2);// kJ/kg
+n_r1=((h_1-h_2)/(h_1-h_f2))*100;// The thermal efficiency of the cycle without feed pump work in %
+//(b)
+W_p=(v_f2*(p_1-p_2)*10^5)/1000;// kJ
+n_r2=(((h_1-h_2)-W_p)/(h_1-(h_f2+W_p)))*100;// The thermal efficiency of the plant feed pump work in %
+printf('\nThe thermal efficiency of the cycle without feed pump work=%0.2f percentage \nThe thermal efficiency of the cycle with feed pump work=%0.2f percentage',n_r1,n_r2);
+// The answer vary due to round off error
+
-- 
cgit