Answer:
(a) To determine the fraction of the air liquefied during expansion, we need to calculate the enthalpy of the low-pressure gas leaving the exchanger and compare it to the enthalpy of saturated liquid at 2 bar. The enthalpy of the low-pressure gas leaving the exchanger can be calculated using the temperature and the enthalpy of the high-pressure gas entering the exchanger:
Enthalpy of low-pressure gas = Enthalpy of high-pressure gas - Heat exchanged with low-pressure gas
= 516 kJ/kg - (526 kJ/kg - 516 kJ/kg)
= 526 kJ/kg
The fraction of the air liquefied during expansion can then be calculated as the difference between the enthalpy of the low-pressure gas and the enthalpy of saturated liquid at 2 bar, divided by the enthalpy of saturated vapour at 2 bar:
Fraction of air liquefied = (526 kJ/kg - 121 kJ/kg) / (314 kJ/kg - 121 kJ/kg)
= 0.48
(b) To determine the temperature of the air on the high-pressure side of the throttle valve, we need to calculate the temperature of the high-pressure gas entering the exchanger and subtract the 14 K approach. The temperature of the high-pressure gas entering the exchanger can be calculated using the enthalpy and the pressure:
Temperature of high-pressure gas = (Enthalpy - Enthalpy of saturated liquid) / (Enthalpy of saturated vapour - Enthalpy of saturated liquid)
* (Temperature of saturated vapour - Temperature of saturated liquid) + Temperature of saturated liquid
= (516 kJ/kg - 121 kJ/kg) / (314 kJ/kg - 121 kJ/kg)
* (226.8 K - 216.5 K) + 216.5 K
= 306 K
The temperature of the air on the high-pressure side of the throttle valve is then:
Temperature of high-pressure gas - Approach temperature
= 306 K - 14 K
= 292 K