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 --- 3831/CH13/EX13.7/Ex13_7.sce | 63 +++++++++++++++++++++++++++++++++++++++++++++ 1 file changed, 63 insertions(+) create mode 100644 3831/CH13/EX13.7/Ex13_7.sce (limited to '3831/CH13/EX13.7/Ex13_7.sce') diff --git a/3831/CH13/EX13.7/Ex13_7.sce b/3831/CH13/EX13.7/Ex13_7.sce new file mode 100644 index 000000000..2822ad70e --- /dev/null +++ b/3831/CH13/EX13.7/Ex13_7.sce @@ -0,0 +1,63 @@ +// Example 13_7 +clc;funcprot(0); +// Given data +n_s_pm1=84.0/100;// The isentropic efficiency of the first turbine +n_s_pm2=80.0/100;// The isentropic efficiency of the second turbine +n_s_p=61.0/100;// The isentropic efficiency of the boiler feed pump +n_s_pm=82/100;// The isentropic efficiency of the prime mover + +// Calculation +// (a) +// Station 1 +p_1=600.0;// psia +T_1=700.0;// °F +h_1=1350.6;// Btu/lbm +s_1=1.5874;// Btu/lbm.R +// Station 2s +p_2=100.0;// psia +p_2s=p_2;// psia +s_2s=s_1;// Btu/(lbm.R) +s_f2=0.4745;// Btu/(lbm.R) +s_fg2=1.1291;// Btu/(lbm.R) +h_f2=298.6;// Btu/lbm +h_fg2=889.2;// Btu/lbm +x_2s=(s_2s-s_f2)/s_fg2;// The dryness fraction +h_2s=h_f2+(x_2s*h_fg2);// Btu/lbm +// Station 3 +p_3=100.0;// psia +T_3=700.0;// °F +x_3=0.00;// The dryness fraction +s_3=1.8035;// Btu/(lbm.R) +h_3=1379.2;// Btu/lbm +// Station 4s +p_4=1.00;// psia +p_4s=p_4;// psia +s_4s=s_3;// Btu/lbm.R +s_f4=0.1326;// Btu/(lbm.R) +s_fg4=1.8455;// Btu/(lbm.R) +h_f4=69.7;// Btu/lbm +h_fg4=1036.4;// Btu/lbm +x_4s=(s_4s-s_f4)/s_fg4;// The dryness fraction +h_4s=h_f4+(x_4s*h_fg4);// Btu/lbm +// Station 5 +p_5=1.00;// psia +x_5=0.00;// The dryness fraction +s_5=0.1326;// Btu/(lbm.R) +h_5=69.7;// Btu/lbm +v_5=0.01614;// ft^3/lbm +// Station 6s +p_6=600;// psia +p_6s=p_6;// psia +s_6s=s_5;// Btu/(lbm.R) +h_6s=72.5;// Btu/lbm +v_6s=0.01614;// ft^3/lbm +h_7s=h_6s+(v_6s*(p_7-p_6)*(144/778.16));// Btu/lbm +h_2=h_1-((h_1-h_2s)*n_s_pm1);// Btu/lbm +h_6=h_5+((v_5*(p_6*p_5)*(144/778.16))/(n_s_p));// Btu/lbm +n_T_wr=((((h_1-h_2s)*n_s_pm1)+((h_3-h_4s)*n_s_pm2)-((v_5*(p_6-p_5)*(144/778.16))/(n_s_p)))/((h_1-h_6)+(h_3-h_2)))*100;// The Rankine cycle thermal efficiency of the plant with reheat in % +// (b) +s_4s=s_1;// Btu/(lbm.R) +x_4s=(s_4s-s_f4)/s_fg4;// The dryness fraction +h_4s=h_f4+(x_4s*h_fg4);// Btu/lbm +n_T_wor=((((h_1-h_4s)*n_s_pm)-((h_6s-h_5)/n_s_pm))/(h_1-h_6))*100;// The Rankine cycle thermal efficiency of the plant without reheat in % +printf("\n(a)The Rankine cycle thermal efficiency of the plant with reheat,n_T=%2.1f percentage \n(b)The Rankine cycle thermal efficiency of the plant without reheat,n_T=%2.1f percentage",n_T_wr,n_T_wor); -- cgit