Refrigerant 134a is throttled from the standard liquid state
Solution
>> Using Property Table for refrigerant R134-a,
>> At P1 = 800 kPa , Saturated Liquid State,
From Table,
h1 = Enthalpy = hf = 95.48 KJ/Kg
T1 = Temperature = 31.31 C
>> Now, As Throttling Process Occurs upto P2 = 200 kPa
As, Under Throttling, Enthalpy remains constant
=> h2 = h1 = 95.48 KJ/Kg
>> Now, Using Table or P2 = 200 kPa and h2 = 95.48 KJ/Kg
T2 = - 10.09 C
and, as hf = 38.41 KJ/Kg
and, hg = 244.50 KJ/Kg
As, h2 = hf + x*(hg - hf)
=> 95.48 = 38.41 + x*(244.50 - 38.41)
=> x = 0.2769
>> Now, Vg = 0.09995 m3/Kg
and, Vf = 0.753*10-3 m3/Kg
>> So, V2 = Vf + x*(Vg - Vf)
=> V2 = 0.753*10-3 + 0.2769*(0.9995 - 0.753*10-3 )
=> V2 = Final Specific Volume of the Refrigerant = 0.2773 m3/Kg ........ANSWER....
and, temperature Drop during this process = T1 - T2 = 31.31 - (- 10.09) = 41.40 C ......ANSWER....
