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Development and multi-objective optimization of geothermal-based organic Rankine cycle integrated with thermoelectric generator and proton exchange membrane electrolyzer for power and hydrogen production

机译:结合热电发生器和质子交换膜电解器生产地热的地热有机朗肯循环的开发和多目标优化

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摘要

The aim of this study is to enhance the performance of a geothermal-based organic Rankine cycle by proposing two novel systems in which some part of the waste heat is recovered employing thermoelectric generator for power and/or hydrogen production (using proton exchange membrane electrolyzer). Accordingly, two novel systems are proposed and analyzed along with the basic organic Rankine cycle (configuration (a)). In the first proposed system, some part of the waste heat is recovered by employing thermoelectric generator (configuration (b)), while in the second one the additional power generated by thermoelectric generator is used in the proton exchange membrane electrolyzer for hydrogen production (configuration (c)). The performances of the proposed systems are investigated and compared with that of the basic cycle from energy, exergy and exergoeconomic viewpoints and are optimized using genetic algorithm via a multi-objective optimization strategy. The results indicate that, at the best solution point obtained from multi-objective optimization, the exergy efficiencies of the proposed systems (configurations (b) and (c)) are higher than that of the basic organic Rankine cycle by 21.9% and 12.7%, respectively. Furthermore, another interesting result is found which reveals that the specific product cost for the proposed configurations (b) and (c) is lower than that for the basic organic Rankine cycle, despite the higher total cost rate for the proposed configurations.
机译:这项研究的目的是通过提出两个新颖的系统来提高基于地热的有机朗肯循环的性能,在该系统中,利用热电发生器回收部分废热,用于发电和/或制氢(使用质子交换膜电解器) 。因此,提出了两个新颖的系统,并与基本的有机朗肯循环(配置(a))一起进行了分析。在第一个提出的系统中,一部分废热通过使用热电发生器来回收(配置(b)),而在第二个系统中,由热电发生器产生的额外功率在质子交换膜电解槽中用于生产氢气(配置(C))。从能源,火用和人类经济角度对所提出系统的性能进行了研究,并与基本周期的性能进行了比较,并通过遗传算法通过多目标优化策略对其进行了优化。结果表明,在通过多目标优化获得的最佳解决方案点上,所提出的系统(配置(b)和(c))的火用效率比基本有机朗肯循环的火用效率高21.9%和12.7%。 , 分别。此外,发现了另一个有趣的结果,该结果表明,尽管所建议的配置的总成本较高,但所建议的配置(b)和(c)的特定产品成本低于基本有机朗肯循环的产品成本。

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