Step 1: State points enthalpies.
- State 1 (compressor inlet): Saturated vapor at 140 kPa.
\[
h_1 = h_g @ 140 \, kPa = 239.19 \, kJ/kg
\]
- State 2 (compressor outlet, isentropic): At 800 kPa. Given superheated $h = 296.82 \, kJ/kg$.
\[
h_2 = 296.82 \, kJ/kg
\]
- State 3 (after condenser, saturated liquid at 800 kPa):
\[
h_3 = h_f @ 800 \, kPa = 95.48 \, kJ/kg
\]
- State 4 (throttling to 140 kPa, isenthalpic):
\[
h_4 = h_3 = 95.48 \, kJ/kg
\]
Step 2: Work and heat interactions.
- Compressor work:
\[
W_{comp} = h_2 - h_1 = 296.82 - 239.19 = 57.63 \, kJ/kg
\]
- Refrigerating effect:
\[
Q_{in} = h_1 - h_4 = 239.19 - 95.48 = 143.71 \, kJ/kg
\]
Step 3: COP of refrigerator.
\[
COP = \frac{Q_{in}}{W_{comp}} = \frac{143.71}{57.63} \approx 2.92
\]
Final Answer:
\[
\boxed{2.92}
\]
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