(ii) `113 L , 0.44 xx 10^(5)N//m^(2)` , (iii)`12459J`
(ii) Process `AB` : `(V_(A))/(T_(A)) = (V_(B))/(T_(B))`
`T_(B) = (V_(B))/(V_(A)) T_(A) = 2T_(A) = 600K`
Process `BC` : `T_(B)V_(B)^(gamma-1) = T_(C)V_(C)^(gamma-1)`
`implies V_(C) = 80sqrt(2) "Litre" = 113L`
For end states A & C `(P_(A).V_(A))/(T_(A)) = (P_(C)V_(C))/(T_(C))= nR implies P_(C) = 0.44 xx 10^(5)N//m^(2)`
(iii) Work done `W_(AB) = P_(A)(2V_(0) -V_(0))= nRT_(A) = 600R, W_(BC) = (nR(T_(B) - T_(C))/(gamma-1)) = (3)/(2)nR (6000-300) = 900R`
