Page 7 of 7 (c) Calculate the heat transfer during this process
(1->3)
. (2 points) (d) Drww the process en the T-v and P-v diagrame with respect to saburation line. (2 points) Page 6 of 7 Problem 4 (10 points) A mass of 2 kg of saturated mbxture of refrigerant (
R-134a
) is cootained in a pidton-cylinder device at
0\deg C
. Initially, 1.5 kg of the refrigerant is in the liquid phase and the 0.5 kg is in the vapor phase. Heat is now transferred to the refligerant, and the piston, which is resting on a set of stops, starts moving When the pressure inside reaches 400 kPa . Heat transfer continues until the total volume increases by 50 percent. Show all weur merk clearly, (a) Fill in the following table with all properties at states
1,2,43
. (4 points) \table[[,
P(kPa)
,
T(\deg C)
,
v((m^(3))/((kg)))
,
V(m^(3))
,
u((kf)/(kg))
,Phase],[State 1,,0,,,,Matare],[State 2,,,,,,],[State 3,,,,,,]] (b) Calculate the work dooe during this peocess
(1->3)
. (2 poinsa)