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1­8 Heat exchangers Heat exchangers can use up to 30% of total ORC cost. They consist of evaporator, regenerator and condenser.22 According to a study 50 higher evaporator pressure results in less overall heat exchanger area in ORC. This includes the total heat transfer area in evaporator, condenser, de‐supper heater (explained in appendix, section: A‐2), and pre‐heater. To increase evaporator pressure, pump should be adjusted in order to give higher pressures in evaporator inlet. Moreover, as already mentioned, reasonable higher evaporator pressure is interesting, since overall turbine size will be decreased and this will bring down the cost. However, excessive high pressures in heat exchangers result in more expensive materials for its manufacturing. Hence, a balance on chosen pressure should be gained. In some applications, it is recommended to keep this pressure bellow 20 bars to prohibit expensive materials for heat exchanger manufacturing (Ulli Drescher, Dieter Bru ̈ggemann, 2007). 1­9 Boilers – evaporators Boilers are normally divided into two sections which are both shell and tube heat exchangers. One is responsible for pre‐heating the liquid working fluid to boiling temperature, while the other section will evaporate it. Normally exhaust gas is in the shell while the ORC working fluid moves in tube side. To avoid corrosion the tube part is from copper or stainless steel and shell part is cylindrical to increase the heat transfer area.22 Vapor and liquid separation is done between boiler shell and casing in outside part. Since only dry vapor is admitted to turbine, a signal from a float control valve will be needed. This will adjust feed pump speed or mass flow recirculation from pump exit to pump inlet in order to control the flow into to boiler and receive dry vapor after boiler. If vapor can be admitted to turbine, a single pass system will be used to give desired wetness of vapor and external recirculation will not be needed any more. In this case, a cheaper type of plate fin can be used. A vapor fraction control system however shall be added. Normally this control system uses a reference data from fluid after turbine. A small fraction of flow from boiler outlet is throttled to condenser inlet. This sample must be supper heated when reaching condenser pressure. By knowing the sample pressure and temperature at condenser inlet its enthalpy is measured. By equating this 50 A.A. Lakew, O. Bolland, Working fluids for low temperature heat source, Applied Thermal Engineering (2010), doi: 10.1016/j.applthermaleng.2010.02.009: Page: 33. 63

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