Answer to Question #236688 in Mechanical Engineering for Klynz1

Question #236688
Steam from a superheater at 7 bar, 300 degree Celsius is mixed in steady adiabatic flow with wet steam at 7 bar, dryness fraction 0.9.calculate the mass of wet steam required per kilogram of superheated steam to produce steam at 7 bar, dry saturated.
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Expert's answer
2021-09-14T01:53:53-0400


We have x amount of superheated steam at 7 bar (700kpa700kpa ) and 300C=>h=3059kj/kg300C=> h=3059kj/kg (h of superheated at temp and press)


total energy of the closed system:

x×3059+y×2556.22=z×2762.8;z=x+yx\times3059+y\times2556.22=z\times2762.8; z=x+y (closed system)

x×3059+y×2556.22=(x+y)×2762.8x\times3059+y\times 2556.22=(x+y)\times2762.8 ; lets assume L is the mass ratioof wet steam to superheated

=> L=y/xL=y/x x(3059+L(2556.22)=x(1+L)2762.8x(3059+L(2556.22)=x(1+L)2762.8

(3059+L×2556.22)=(1+L)×2762.8(3059+L\times2556.22)=(1+L)\times2762.8

solve for L and you should get 1.43kg1.43 kg wet steam/kg superheated (itwill be a little off because my steam tables might be different orrounding)


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