Exergoeconomic analysis and multi-objective optimization of an ejector refrigeration cycle powered by an internal combustion (HCCI) engine

•Ejector refrigeration systems powered by HCCI engine is proposed.•A new two-dimensional model is developed for the ejector.•Multi-objective optimization is performed for the proposed system.•Pareto frontier is plotted for multi-objective optimization. Ejector refrigeration systems powered by low-gr...

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Veröffentlicht in:Energy conversion and management 2015-05, Vol.96, p.403-417
Hauptverfasser: Sadeghi, Mohsen, Mahmoudi, S.M.S., Khoshbakhti Saray, R.
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Sprache:eng
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Zusammenfassung:•Ejector refrigeration systems powered by HCCI engine is proposed.•A new two-dimensional model is developed for the ejector.•Multi-objective optimization is performed for the proposed system.•Pareto frontier is plotted for multi-objective optimization. Ejector refrigeration systems powered by low-grade heat sources have been an attractive research subject for a lot of researchers. In the present work the waste heat from exhaust gases of a HCCI (homogeneous charge compression ignition) engine is utilized to drive the ejector refrigeration system. Considering the frictional effects on the ejector wall, a new two-dimensional model is developed for the ejector. Energy, exergy and exergoeconomic analysis performed for the proposed system using the MATLAB software. In addition, considering the exergy efficiency and the product unit cost of the system as objective functions, a multi-objective optimization is performed for the system to find the optimum design variables including the generator, condenser and evaporator temperatures. The product unit cost is minimized while the exergy efficiency is maximized using the genetic algorithm. The optimization results are obtained as a set of optimal points and the Pareto frontier is plotted for multi-objective optimization. The results of the optimization show that ejector refrigeration cycle is operating at optimum state based on exergy efficiency and product unit cost when generator, condenser and evaporator work at 94.54°C, 33.44°C and 0.03°C, respectively.
ISSN:0196-8904
1879-2227
DOI:10.1016/j.enconman.2015.02.081