diff options
Diffstat (limited to '3685/CH12/EX12.6/Ex12_6.sce')
-rw-r--r-- | 3685/CH12/EX12.6/Ex12_6.sce | 55 |
1 files changed, 55 insertions, 0 deletions
diff --git a/3685/CH12/EX12.6/Ex12_6.sce b/3685/CH12/EX12.6/Ex12_6.sce new file mode 100644 index 000000000..4aaa681d3 --- /dev/null +++ b/3685/CH12/EX12.6/Ex12_6.sce @@ -0,0 +1,55 @@ +clc +h1 = 3023.5 // Enthalpy of steam at state 1 in kJ/kg +s1 = 6.7664 // Enthalpy of steam at state 1 in kJ/kgK +s2 = s1 // Isentropic process +s3 = s1 //Isentropic process +s4 = s1 //Isentropic process +t_sat_20 = 212 // Saturation temperature at 20 bar in degree Celsius +t_sat_1 = 46 // Saturation temperature at 1 bar in degree Celsius +dt = t_sat_20-t_sat_1 // Change in temperature +n =3 // number of heaters +t = dt/n // temperature rise per heater +t1 = t_sat_20-t // Operational temperature of first heater +t2 = t1-t// Operational temperature of second heater +// 0.1 bar +hf = 191.83 // Enthalpy of fluid in kJ/kg +hfg = 2392.8 // Latent heat of vaporization in kJ/kg +sf = 0.6493// Entropy of fluid in kJ/kgK +sg = 8.1502// Entropy of gas in kJ/kgK +// At 100 degree +hf100 = 419.04 // Enthalpy of fluid in kJ/kg +hfg100 = 2257.0// Latent heat of vaporization in kJ/kg +sf100 = 1.3069 // Entropy of fluid in kJ/kgK +sg100 = 7.3549 // Entropy of gas in kJ/kgK +// At 150 degree +hf150 = 632.20 // Enthalpy of fluid in kJ/kg +hfg150 = 2114.3// Latent heat of vaporization in kJ/kg +sf150 = 1.8418 // Entropy of fluid in kJ/kgK +sg150 = 6.8379// Entropy of gas in kJ/kgK +x2 = (s1-sf150)/4.9961 // Steam quality +h2 = hf150+(x2*hfg150) // Enthalpy at state 2 in kJ/kg +x3 = (s1-sf100)/6.0480 // Steam quality +h3 = hf100+(x3*hfg100) // Enthalpy at state 3 in kJ/kg +x4 = (s1-sf)/7.5010 // Steam quality +h4 = hf+(x4*hfg)//Enthalpy at state 4 in kJ/kg +h5 = hf // Enthalpy at state 5 in kJ/kg +h6 = h5 //Enthalpy at state 6 in kJ/kg +h7 = hf100 // Enthalpy at state 7 in kJ/kg +h8 = h7 // Enthalpy at state 8 in kJ/kg +h9 = 632.2 // Enthalpy at state 9 in kJ/kg +h10 = h9 // Enthalpy at state 10 in kJ/kg +m1 = (h9-h7)/(h2-h7) // regenerative mass +m2 = ((1-m1)*(h7-h6))/(h3-h6) // regenerative mass +Wt = 1*(h1-h2)+(1-m1)*(h2-h3)+(1-m1-m2)*(h3-h4) // Turbine work +Q1 = h1-h9 // Heat addition +Wp = 0 // Pump work is neglected +n_cycle = 100*(Wt-Wp)/Q1 // Cycle efficiency +sr = 3600/(Wt-Wp) // Steam rate + +printf("\n Example 12.6\n") +printf("\n Steam quality at turbine exhaust is %f ",x3) +printf("\n Net work per kg of stem is %f kJ/kg",Wt) +printf("\n Cycle efficiency is %f percent",n_cycle) +printf("\n Stream rate is %f kg/kW h",sr) +//The answers vary due to round off error + |