for P= 36.29 bar,. h₁ = hg =2801.7 h4 = hf = 1057.5 k31kg hfg 1744.2 kJ/kg 43149 T = 244.2 C = 517.2K. .5,' = sg = 6.111 kJ/kg K '= 2.740 kJ/kg. 54= •We have s₁ =52. • 7.080 = S,' + Cvapor in (I+). 7.080 = 6.111+ 2.1 In (STA-2) T= 820.45 K. hh,+Cvapor CT, T₁) hi = 2801.7 + 2.1 (820.45-517.2) h₁ =3438.53 kJ/kg CS Scanned with CamScanner Cp water = 2.1 kJ/kg k 171 for hy Wp = √3 (P4-P3) 0.001065 (36.29-2.26) 30% To produce more power the upper management decided to modify the power plant by placing the stage 2 as a saturated liquid stage. The condenser site was planned to leave as it is with the same parameters. The flow rates stays the same. See the figure below for the data. Again, this an ideal case: S2-S1; S3=54. Boiler P1=36.29bar lin Draw: The T-S diagram of the cycle Turbine Condenser Pump P2=2.26 bar -2 Saturated vapor T6=? 6 Lour T5=15C 5 Cooling water 3 saturated liquid
for P= 36.29 bar,. h₁ = hg =2801.7 h4 = hf = 1057.5 k31kg hfg 1744.2 kJ/kg 43149 T = 244.2 C = 517.2K. .5,' = sg = 6.111 kJ/kg K '= 2.740 kJ/kg. 54= •We have s₁ =52. • 7.080 = S,' + Cvapor in (I+). 7.080 = 6.111+ 2.1 In (STA-2) T= 820.45 K. hh,+Cvapor CT, T₁) hi = 2801.7 + 2.1 (820.45-517.2) h₁ =3438.53 kJ/kg CS Scanned with CamScanner Cp water = 2.1 kJ/kg k 171 for hy Wp = √3 (P4-P3) 0.001065 (36.29-2.26) 30% To produce more power the upper management decided to modify the power plant by placing the stage 2 as a saturated liquid stage. The condenser site was planned to leave as it is with the same parameters. The flow rates stays the same. See the figure below for the data. Again, this an ideal case: S2-S1; S3=54. Boiler P1=36.29bar lin Draw: The T-S diagram of the cycle Turbine Condenser Pump P2=2.26 bar -2 Saturated vapor T6=? 6 Lour T5=15C 5 Cooling water 3 saturated liquid
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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Problem 1.1MA
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please explain how to obtain those values, how you get alll the values in the imagine.
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