1. The problem statement, all variables and given/known data A coal-fired steam power plant operates on the ideal Rankine cycle. Feedwater from the condenser at P1= 10 kPa is pumped to the boiler at P2= P3 = 20 MPa, where it is superheated and exits the boiler at T3 = 550 °C. The moisture content in the turbine is not to exceed 12% (i.e. steam quality is to be maintained above x = 0.88 throughout the turbine). Up to two reheat stages can be added to the steam cycle to satisfy this requirement. If needed, one stage can be added to reheat the steam to T5 = 525 °C at P4 = P5 = 10 MPa. If more reheating is required, a second stage can be added to reheat the steam to T7= 500 °C at P6= P7 = 2.5 MPa. (a). How many reheat stages are required for this power plant (no reheat, single reheat, or double reheat)? Provide calculations in support of your answer. (b). What is the thermal efficiency ηth of the power cycle? (c). Determine the annual emission of sulfur dioxide, mSO2, in metric tons, from this power plant, if the net generating capacity of the plant is 600 MW, and the boiler is 88% efficient in transferring combustion heat into the feedwater superheat and steam reheat stages. The boiler burns, to completion, Power River Basin coal that has a heating value of 22,800 kJ/kg and contains 0.46 wt% sulfur. Assume that all of the sulfur content of the coal is emitted as SO2 in the combustion flue gas, and that the coal-burning plant has a capacity factor of 0.85; i.e. the boiler is operational for 85% of the hours in one calendar year. (1 metric ton = 1000 kg) 2. Relevant equations Energy balance equations. 3. The attempt at a solution I completed the first 2 parts of the problem and I found out that one reheating stage is enough to active a steam quality more than 88.2%. I also calculated the thermal efficiency of 38/6% of this power plant. My question is about part 3. How can I approach?