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and high pressure ORC fluid enters the ORC evaporator at point 26 to close the ORC power generation unit. Since flue gases leaving the ORC evaporator still have energy, a domestic water heater is used to utilize the energy of the hot gases at point 33. Water enters the domestic water heater at point 35 and hot water leave the domestic water heater at point 36. Reverse osmosis (RO) desalination is used to produce fresh water as shown right bottom side of Fig. 4.2. Sea water at point 37 enters a filter to remove dissolved species and then passes through the absorber of the double-effect absorption chiller to increase the temperature to improve the efficiency of the OR desalination unit. A high pressure RO pump is used to increase the pressure of the water. High pressure sea water leaves the RO pump and enters the RO unit at point 40. Fresh water is produced at point 41 and stored in a fresh water tank for the later use while high pressure brine water enters a hydraulic turbine to reduce the pressure and generate electricity. Finally, low pressure brine water leaves the RO unit and sends back to the sea. The cooling load of the system is provided by a double-effect absorption chiller. Weak Li-Br solution at point a is pumped through an high pressure solution leaves the pump at point 2 then passes through a high temperature heat exchanger to increase the temperature. High temperature weak solution then enters the high temperature heat exchanger at point 3 and the high temperature weak solution enters the high temperature generator. In high temperature generator water is removed from the solution and the strong solution sends back to the absorber after passing through the high and low temperature heat exchangers. On the other side, vapor leaves the high temperature generator at point 17 and enters the low temperature generator. The refrigerant steam produced by the low pressure generator is condensed by the cooling water and then enters the expansion valve at point 8 to reduce the pressure and enters the evaporator at point 9. This low pressure vapor enters the evaporator and saturated vapor leaves the evaporator at point 10 and enters the absorber. The absorption heat is removed by the sea water entering the absorber at point 38 to improve the efficiency of the RO desalination unit. 53PDF Image | Energy Systems for Multigeneration Purposes
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