Temperature of source, T1 = 250 + 273 = 523 K
Temperature of sink, T2 = – 15 + 273 = 258 K
Heat received by the system, Q1 = 90 kJ
ηcarnot = 1 – \(\cfrac{T_2}{T_1}\) = 1 - \(\cfrac{258}{523}\)
= 0.506 = 50.6%.
(ii) The net work transfer, W = ηcarnot × Q1

= 0.506 × 90 = 45.54 kJ.
(iii) Heat rejected to the sink, Q2 = Q1 – W
[\(\because\) W = Q1 – Q2]
= 90 – 45.54 = 44.46 kJ.