diff options
Diffstat (limited to '32/CH8/EX8.04/8_04.sce')
-rwxr-xr-x | 32/CH8/EX8.04/8_04.sce | 46 |
1 files changed, 46 insertions, 0 deletions
diff --git a/32/CH8/EX8.04/8_04.sce b/32/CH8/EX8.04/8_04.sce new file mode 100755 index 000000000..e12088ca4 --- /dev/null +++ b/32/CH8/EX8.04/8_04.sce @@ -0,0 +1,46 @@ +//pathname=get_absolute_file_path('8.04.sce')
+//filename=pathname+filesep()+'8.04-data.sci'
+//exec(filename)
+//Pressure of the steam entering(in MPa):
+p1=20
+//Temperature(in K):
+T1=500+273
+//Dryness fraction of the steam leaving:
+x=0.90
+//Condensor pressure(in MPa):
+p6=0.005
+//From steam tables:
+h2=3238.2 //kJ/kg
+s2=6.1401 //kJ/kg.K
+s3=s2
+hf=137.82 //kJ/kg
+hfg=2423.7 //kJ/kg.K
+sf=0.4764 //kJ/kg.K
+sfg=7.9187 //kJ/kg.K
+h6=137.82 //kJ/kg
+h4=3474.1 //kJ/kg
+sf1=2.2842 //kJ/kg.K
+sfg1=4.1850 //kJ/kg.K
+hf1=830.3 //kJ/kg
+hfg1=1959.7 //kJ/kg
+v6=0.001005 //m^3/kg
+//Enthalpy at state 5(in kJ/kg):
+h5=hf+x*hfg
+s5=sf+x*sfg
+//By interpolation, pressure at state 4(in bar):
+p4=1.4
+//Dryness fraction at state 3:
+x3=(s3-sf1)/sfg1
+//Enthalpy at state 3(in kJ/kg):
+h3=hf1+x3*hfg1
+//Enthalpy at state 1(in kJ/kg):
+h1=h6+v6*(p1-p6)*10^3
+//Net work per kg of steam(in kJ/kg):
+Wnet=(h2-h3)+(h4-h5)-(h1-h6)
+//Heat added per kg of steam(in kJ/kg):
+Q=h2-h1
+//Thermal efficiency:
+n=Wnet/Q*100
+printf("\n RESULT \n")
+printf("\nPressure of steam leaving HP turbine = %f MPa",p4)
+printf("\nThermal efficiency = %f percent",n)
\ No newline at end of file |