Please answer it perfectly, to the point and correct, I will upvote, try your best. Steam is generated in the boiler at a chemical site power station at 30 bara and superheated to 300°C. This steam is expanded through a turbine used to drive a compressor, which requires 6 MW of shaft power. The turbine has an isentropic efficiency of 60% and expands to a pressure of 5 bara. The steam then passes to a vapor-liquid separator with the top product entering the site LP steam main. If the stream entering the separator is two-phase, what is the flow of water from the V/L separator? If the V/L separator is vapor only, how much boiler feed water at 96°C could you spray into the stream before it enters the separator to maximize the amount of steam exported to the LP steam main?