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author | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
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committer | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
commit | 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch) | |
tree | dbb9e3ddb5fc829e7c5c7e6be99b2c4ba356132c /3733/CH22/EX22.12 | |
parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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-rw-r--r-- | 3733/CH22/EX22.12/Ex22_12.sce | 27 |
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diff --git a/3733/CH22/EX22.12/Ex22_12.sce b/3733/CH22/EX22.12/Ex22_12.sce new file mode 100644 index 000000000..29894dd0f --- /dev/null +++ b/3733/CH22/EX22.12/Ex22_12.sce @@ -0,0 +1,27 @@ +// Example 22_12
+clc;funcprot(0);
+//Given data
+T_1=300;// °C
+p_1=35;// bar
+p_2=25;// bar
+p_2a=1.5;// bar
+p_3=0.1;// bar
+n_t=80/100;// The isentropic efficiency for both sections of the turbine
+gradT=10;// °C
+m_w=1;// kg
+C_p=4.2;// kJ/kg.°C
+
+// Calculation
+// From h-s chart:
+h_1=2970;// kJ/kg
+h_2=2504;// kJ/kg
+h_3=2197;// kJ/kg
+h_f2=264;// kJ/kg (at 1.5 bar)
+h_f2a=h_f2-(m_w*C_p*gradT);// kJ/kg
+h_f3=190;// kJ/kg (at 0.1 bar)
+m=(h_f2a-h_f3)/(h_2-h_f3);// kg/kg of steam
+W=(h_1-h_2)+((1-m)*(h_2-h_3));// kJ/kg
+Q_s=h_1-h_f2a;// kJ/kg
+n_th=(W/Q_s)*100;// Thermal efficiency of the plant
+printf('\n(a)Bleed steam per kg of steam supplied to the steam turbine=%0.3f kg/kg of steam \n(b)The thermal efficiency of the plant=%0.1f percentage',m,n_th);
+// The answer provided in the textbook is wrong
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