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An important conclusion is that minimum exergy consumption (or maximum exergy production) can be achieved when expansion starts at pinch temperatures or ambient temperature.
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It is also observed that the system favors a lower ambient temperature for maximum exergy efficiency and hydrogen production.
The obtained optimal configuration presented maximum exergy efficiency, hydrolyzed bagasse fraction, capital costs and ethanol production rate, and minimum cooling water consumption and power production rate.
The effect of perfect cooling after regeneration leads to a gain of 7.4% in maximum exergy efficiency and 20% in maximum power output.
Two single-objective optimizations were conducted to reach the maximum exergy efficiency and the minimum average levelized costs per unit of exergy products for the overall system, respectively.
However, the methanol has the minimum exergy efficiency and the maximum exergy destruction.
Maximum exergy efficiency was obtained 66.8% while minimum exergy efficiency was 31.6%.
The results demonstrated that the methane has the maximum exergy efficiency and the minimum exergy destruction.
The objective is to minimize exergy consumption (or maximize exergy production).
The system has 43% maximum energy efficiency and 65% maximum exergy efficiency.
Exergy analysis indicates that maximum exergy is destroyed in HCCI engine which represents about 90.09% of the total exergy destruction in the overall system.
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Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com