Answer:
P2 = 3.9 MPa
Explanation:
Given that
T₁ = 290 K
P₁ = 95 KPa
Power P = 5.5 KW
mass flow rate = 0.01 kg/s
solution
with the help of table A5
here air specific heat and adiabatic exponent is
Cp = 1.004 kJ/kg K
and k = 1.4
so
work rate will be
W = m × Cp × (T2 - T1) ..........................1
here T2 = W ÷ ( m × Cp) + T1
so T2 = 5.5 ÷ ( 0.001 × 1.004 ) + 290
T2 = 838 k
so final pressure will be here
P2 = P1 ×
..............2
P2 = 95 × 
P2 = 3.9 MPa
Answer:

Explanation:
The mixing chamber can be modelled by applying the First Law of Thermodynamics:

Since that mass flow rate of water at inlet 1 is the only known variable, the expression has to be simplified like this:

Besides, the following expression derived from the Principle of Mass Conservation is presented below:

Then, the expression is simplified afterwards:


Specific enthalpies are obtained from steam tables and described as follows:
State 1 (Superheated vapor)

State 2 (Saturated liquid)

State 3 (Liquid-Vapor mixture)

The ratio of the stream at state 2 to the stream at state 1 is:



The mass flow rate of the saturated liquid is:



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