diff options
Diffstat (limited to '32/CH13/EX13.14')
-rwxr-xr-x | 32/CH13/EX13.14/13_14.sce | 61 |
1 files changed, 61 insertions, 0 deletions
diff --git a/32/CH13/EX13.14/13_14.sce b/32/CH13/EX13.14/13_14.sce new file mode 100755 index 000000000..e2794cdf2 --- /dev/null +++ b/32/CH13/EX13.14/13_14.sce @@ -0,0 +1,61 @@ +//pathname=get_absolute_file_path('13.14.sce')
+//filename=pathname+filesep()+'13.14-data.sci'
+//exec(filename)
+//Mass flow rate(in kg/s):
+m1=150/60
+//Height of water level from the axis of injector(in m):
+H=5
+//Pressuer at which steam is injected(in bar):
+p4=20
+//Water level in boiler from the injector(in m):
+Z4=0.8
+//Dryness fraction at state 1:
+x1=0.95
+//Velocity in delivery pipe(in m/s):
+C4=20
+//Atmospheric pressure(in bar):
+p3=1.013
+//Density(in kg/m^3):
+d=10^3
+//Acceleration due to gravity(in m/s^2):
+g=9.81
+//Specific heat of steam(in kJ/kg.K):
+Cps=3.18
+//Specific heat of water(in kJ/kg.K):
+Cpw=4.18
+//From steam tables:
+T1=212.42 //C
+Tw=25 //C
+p2=0.7*p4
+h1=2704.95 //kJ/kg
+hfg1=1890.7 //kJ/kg
+s1=6.1462 //kJ/kg.K
+s2=s1
+x2=0.923
+h2=2639.10 //kJ/kg
+v2=0.13 //m^3/kg
+//Velocity of steam at throat(in m/s):
+C2=sqrt(2*(h1-h2)*10^3)
+//Velocity at state 3(in m/s):
+C3=sqrt(2*(g*Z4+p4*10^5/d+C4^2/2-p3*10^5/d))
+//Mass of water pumped per kg of steam(in kg):
+m=(C2-C3)/(sqrt(2*g*H)+C3)
+printf("\nRESULT\n")
+printf("\nMass of water pumped per kg of steam = %f kg",m)
+//Mass of mixture passing through state 3(in kg/s):
+m3=m1+m1/m
+//Area of throat of mixing nozzle(in cm^2):
+A3=m3/(d*C3)*10^4
+//Diameter of throat of the mixing nozzle(in cm):
+d3=sqrt(A3*4/%pi)
+printf("\nDiameter of throat of the mixing nozzle = %f cm",d3)
+//Mass of steam required for given flow rate(in kg/s):
+ms=m1/m
+//Area at state 2(in cm^2):
+A2=ms*v2/C2*10^4
+//Diameter of throat of steam nozzle(in cm):
+d2=sqrt(A2*4/%pi)
+printf("\nDiameter of throat of steam nozzle = %f cm",d2)
+//Temperature of water coming out of the injector(in C):
+T3=(x1*hfg1+Cps*T1+m*Cpw*Tw)/(m*Cpw+Cps)
+printf("\nTemperature of water coming out of the injector = %f C",T3)
\ No newline at end of file |