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Diffstat (limited to '3831/CH13/EX13.4/Ex13_4.sce')
-rw-r--r-- | 3831/CH13/EX13.4/Ex13_4.sce | 44 |
1 files changed, 44 insertions, 0 deletions
diff --git a/3831/CH13/EX13.4/Ex13_4.sce b/3831/CH13/EX13.4/Ex13_4.sce new file mode 100644 index 000000000..bb8089c27 --- /dev/null +++ b/3831/CH13/EX13.4/Ex13_4.sce @@ -0,0 +1,44 @@ +// Example 13_4
+clc;funcprot(0);
+// Given data
+D=40.0;// inch
+L=10.0;// ft stroke
+W_actual=1400;// hp
+n=36.0;// rpm
+n_s_p=0.650;// The isentropic efficiency of a pump
+n_s_pm=0.550;// The isentropic efficiency of an engine
+d_fw=30.0;// The diameter of the flywheel in ft
+w=56.0;/// tons
+
+// Calculation
+// (a)
+// Station 1-Engine inlet
+p_1=100.0;// psia
+x_1=1.00;// The quality of steam at Station 1
+h_1=1187.8;// Btu/lbm
+s_1=1.6036;// Btu/lbm.R
+// Station 2s-Engine exit
+p_2s=14.7;// psia
+s_2s=s_1;// Btu/lbm.R
+s_f2=0.3122;// Btu/lbm.R
+s_fg2=1.4447;// Btu/lbm.R
+x_2s=(s_2s-s_f2)/s_fg2;// The quality of steam at Station 2s
+h_f2=180.1;// Btu/lbm
+h_fg2=970.4;// Btu/lbm
+h_2s=h_f2+(x_2s*h_fg2);// Btu/lbm
+// Station 3-Condenser exit
+p_3=p_2s;// psia
+x_3=0;// The quality of steam at Station 3
+h_3=h_f2;// Btu/lbm
+v_3=0.01672;// ft^3/lbm
+// Station 4s-Boiler inlet
+p_4s=p_1;// psia
+// s_4s=s_3;
+n_T_max=((h_1-h_2s-(v_3*(p_4s-p_3)))*(144/118.16))/((h_1-h_3-(v_3*(p_4s-p_3)))*(144/118.16));// The maximum isentropic efficiency of the system
+n_T_max=n_T_max*100;// %
+// (b)
+n_T_Rankine=(((h_1-h_2s)*n_s_pm)-((v_3*(p_4s-p_3)/n_s_p)*(144/118.16)))/((h_1-h_3)-((v_3*(p_4s-p_3)/n_s_p)*(144/118.16)));// The isentropic efficiency of the Rankine system
+n_T_Rankine=n_T_Rankine*100;// %
+// (c)
+mdot=(W_actual*2545)/((h_1-h_2s)*n_s_pm);// lbm/h
+printf("\n(a)The maximum isentropic efficiency of the Rankine system,(n_T)_maximum Rankine=%2.1f percentage \n(b)The isentropic efficiency of the Rankine system,(n_T)_Rankine=%1.2f percentage \n(c)The mass flow rate of steam required,mdot=%5.0f lbm/h",n_T_max,n_T_Rankine,mdot);
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