Thank you!

A chemical plant has a high temperature (200C) and pressure ( 60bar) stream of CO2(5.9kg/s) that would normally be exhausted to the atmosphere. They are considering using this stream to run a turbine. The properties of the feed are: V=0.01411m3/kg,U=449.4kJ/kg,H=534.04kJ/kg,S=1.6913kJ/kgK The turbine exhausts at 4 bar. Limited data is available: At 20C V=0.11538m3/kg,U=305.3kJ/kg,H=351.46kJ/kg,S=1.6646kJ/kgK At 12C : V=0.11956m3/kg,U=310.7kJ/kg,H=358.47kJ/kg,S=1.6913kJ/kgK At 0C: V=0.12552m3/kg,U=318.3kJ/kg,H=368.51kJ/kg,S=1.7295kJ/kgK At 20C V=0.13551m3/kg,U=331.57kJ/kg,H=385.77kJ/kg,S=1.7904kJ/kgK If the turbine is 92% efficient, what is the entropy generated (in kW/K ) by this process? Please give your answer to the 0.001 place