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The ratio of net power output to the total heat exchanger area is used as the objective function.
The pressure ratio and the available heat exchanger area allocation are selected optimally so that system performance is maximized.
Therefore, the pressure drop aspect should be considered together with the costs for heat exchanger area and utility consumption.
The least heat exchanger area required at constant power rating is found when the working fluid is n-pentane.
In this paper the interrelationship between HRL storage temperatures, heat recovery and total HRL exchanger area is investigated.
The main objective in this article is to find new exchanger area for the previously found optimum configurations.
Similar(9)
Furthermore, the optimization procedure dramatically reduced the SOFC active area and the compact heat exchanger areas.
Additionally, optimum heat exchanger areas with corresponding optimum operating temperatures are determined.
The experimental investigations include charging and discharging processes at different inlet temperatures and for different heat exchanger areas.
Also, inputs such as heat exchanger areas, compressor design point, etc., were linked in from the Aspen Plus reforming design model.
The optimal temperatures of the working fluids, the optimum performance coefficient, the optimum specific heating load and the optimal distribution of the heat exchanger areas are determined in terms of technical and economical parameters.
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