From b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b Mon Sep 17 00:00:00 2001 From: priyanka Date: Wed, 24 Jun 2015 15:03:17 +0530 Subject: initial commit / add all books --- 2705/CH10/EX10.8/Ex10_8.sce | 63 +++++++++++++++++++++++++++++++++++++++++++++ 1 file changed, 63 insertions(+) create mode 100755 2705/CH10/EX10.8/Ex10_8.sce (limited to '2705/CH10/EX10.8') diff --git a/2705/CH10/EX10.8/Ex10_8.sce b/2705/CH10/EX10.8/Ex10_8.sce new file mode 100755 index 000000000..f65703173 --- /dev/null +++ b/2705/CH10/EX10.8/Ex10_8.sce @@ -0,0 +1,63 @@ +clear; +clc; +disp('Example 10.8'); + +// aim : To determine +// (a) the rankine fficiency +// (b) the specific steam consumption +// (c) the carnot efficiency of the cycle + +// given values +P1 = 1100;// steam entering pressure, [kN/m^2] +T1 = 273+250;// steam entering temperature, [K] +P2 = 280;// pressure at point 2, [kN/m^2] +P3 = 35;// pressure at point 3, [kN/m^2] + +// solution +// (a) +// from steam table, at P1 and T1 is +hf1 = 2943;// [kJ/kg] +hg1 = 2902;// [kJ/kg] +h1 = hf1-.1*(hf1-hg1); // [kJ/kg] + +sf1 = 6.926;// [kJ/kg K] +sg1 = 6.545;// [kJ/kg K] +s1 = sf1-.1*(sf1-sg1);// [kJ/kg K] + +// at P2 +sf2 = 1.647;// [kJ/kg K] + sg2 = 7.014;// [kJ/kg K] +// s2=sf2+x2(sg2-sf2) +// since expansion through turbine is isentropic so s1=s2 + // hence + s2 = s1; + x2 = (s2-sf2)/(sg2-sf2);// dryness fraction + + // at point 2 + hf2 = 551.4;// [kJ/kg] + hfg2 = 2170.1;// [kJ/kg] + h2 = hf2+x2*hfg2;// [kJ/kg] + vg2 = .646;// [m^3/kg] + v2 = x2*vg2;// [m^3/kg] + + // by Fig10.20. + A6125 = h1-h2;// area of 6125, [kJ/kg] + A5234 = v2*(P2-P3);// area 5234, [kJ/kg] + W = A6125+A5234;// work done + hf = 304.3;// specific enthalpy of water at condenser pressuer, [kJ/kg] + ER = h1-hf;// energy received, [kJ/kg] + Re = W/ER;// rankine efficiency + mprintf('\n (a) The rankine efficiency is = %f percent\n',Re*100); + + // (b) + kWh = 3600;// [kJ] + SSC = kWh/W;// specific steam consumption, [kJ/kWh] + mprintf('\n (b) The specific steam consumption is = %f kJ/kWh\n',SSC); + + // (c) + // from steam table +T3 = 273+72.7;// temperature at point 3 +CE = (T1-T3)/T1;// carnot efficiency +mprintf('\n (c) The carnot efficiency of the cycle is = %f percent\n',CE*100); + +// End -- cgit