(a) A water pump has an inlet conditions of 4.55 MPa and 20oC. The outlet of the pump is at a pressure of 18.00 MPa. What is the enthalpy change across a reversible pump in kJ/kg?
(b) For a real system, which of the following pumps might be considered for the job?
12.80 kJ/kg
13.48 kJ/kg
14.18 kJ/kg
(c) If a real pump for the states given in (a) has and efficiency of 0.78, what would be the enthalpy change of water through the pump?
A) Here we will make use of water property table to evaluate enthalpy and any other required data
At inlet conditions of 4.55 MPa and T = 20oC
Hin =88.1911575850 KJ/Kg
Now energy transfer through pumps is generally an isothermal process and also for liquid there is hardly any increase in temperature due to pressurization
at outlet at P = 18 MPa and T =20 oC
Hout =100.7207 KJ/Kg
Enthalpy transfer = Hout - Hin = 100.7207 -88.1911 = 12.5296 KJ/Kg
b) From the option provided, the first option is closest to 12.5296 KJ/Kg,
Hence first option 12.80 KJ/Kg pump can be selected
c) Now efficiency of the pump is 0.78
so only 78 % of the enthalpy has been transferred through the pump
Hence enthalpy change =0.78*12.526 =9.77 KJ/Kg
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