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University of Ottawa *

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2130

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Mechanical Engineering

Date

Oct 30, 2023

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1

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We have a flow of 3 kg/s superheated steam at 300 kPa, 300°C that we want to desuperheat by mixing it with liquid water at 300 kPa, 90°C so that the output is a flow of saturated steam at 300 kPa. Assume the mixing chamber is insulated and find the flow rate of liquid water needed for the process. Control volume: Mixing chamber, similar to Fig. 4.13. Process: Steady-state adiabatic mixing. Inlet, exit states: States 1, 2, and 3 all known. Model: Steam tables, so hy =3069.28kJ/kg; hy =376.9kI/kg; h3 = 2967.59k]/kg Analysis For this situation the unknown is m1,, so the continuity equation gives the output flow rate as M3 = my + my which we substitute into the energy equation as 0 = r1hy + mizhy (i mp)hs
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