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Table 1 Parameter inputs Parameter Day Ta Te mDHS Q ̇FPC Q ̇FPAB Power rating Q ̇ ORCRAT ED Q ̇ O R C I N Electric efficiency, net Value 1 41 [°C] 105 [°C] 85.5424 [kg/s] 14 [MWth ] 3.3408 [MWth ] 1 MWe 10 [MWth ] 10 [MWth ] 0.95 ·(0.16738 − 0.0010936 · T4) Table 2 Parameter outputs for the 20th iteration Parameter Total number of iterations mDHS m mORC mab Ta Tb T4 Tc Td Tab Te This yields Value 20 85.5424 [kg/s] Parameter Q ̇FPC Q ̇FPAB Q ̇HX−FPC Q ̇HX−FPAB Q ̇FGC−FPC Q ̇FGC−FPAB Q ̇ O R C − I N ηel Pel Q ̇ O R C − O U T Total system power - IN Total system power - OUT Value 14 [MWth] 3.8786 [MWth ] 4 [MWth] 3.8786 [MWth ] 4.5858 [MWth ] 1.1831 [MWth ] 10 [MWth] 6.6676 % 0.66676 [MWe ] 69.217 69.217 16.325 41 [°C] 56.812 88.993 88.993 102.79 115 [°C] 115.12 [°C] [kg/s] [kg/s] [kg/s] [°C] [°C] [°C] [°C] 9.3332 22.981 22.981 [MWth ] [MWth ] [MWth ] (2) (3) (4) m ̇ =m ̇DHS −m ̇ab The temperature of the DHS mass flow after FGC-FPC is then calculated as Q ̇FGC−FPC 4.5858·106 Tb =Ta + Cp ·m = 4190·69.217 =41+15.812=56.812°C In order to maximize the mass flow through the ORC condenser, let m ̇ orc = m ̇ = 69.217 kg s =69.217 kg s In order to compute the electric efficiency of the ORC, we need the temperature of mass flow exiting the condenser. In the iterative computation algorithm, the value of the previous iteration is used, 97PDF Image | Analysis of Organic Rankine Cycles for a Boiler Station
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