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Parametric study and optimization of an ejector-expansion TRCC cycle integrated with a water purification system

机译:与净水系统集成的喷射器-扩展TRCC循环的参数研究和优化

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A combined cogeneration cycle is proposed in which the waste heat from an ejector-expansion trans-critical CO_2 refrigeration cycle is utilized for power production and water purification simultaneously. The waste heat utilization was performed by means of a CO_2 supercritical power cycle and a desalination system for pure water production. In order to run the desalination system, an absorption heat transformer is employed to upgrade the lower temperature waste heat. Thermodynamic models are developed for both the ejector-expansion trans-critical CO_2 cycle and the combined cogeneration cycle consisting of all the above mentioned cycles. A parametric study is conducted to investigate and optimize the performance of each cycle under various operating conditions. It is found that, at the optimum conditions, the energy efficiency ratio of combined cogeneration cycle is about 13-45% higher than the coefficient of performance of the ejector-expansion trans-critical CO_2 cycle. It is also concluded that, as the gas cooler temperature increases, the pure water production rate in the combined cogeneration cycle is increased.
机译:提出了联合热电联产循环,其中来自喷射器-膨胀跨临界CO_2制冷循环的废热被同时用于发电和水净化。废热利用是通过CO_2超临界功率循环和用于纯水生产的脱盐系统进行的。为了运行脱盐系统,采用了吸收式热转换器来升级较低温度的废热。针对喷射器-膨胀跨临界CO_2循环以及由所有上述循环组成的联合热电联产循环开发了热力学模型。进行了参数研究,以研究和优化各种操作条件下每个循环的性能。发现在最佳条件下,联合热电联产循环的能效比比喷射器-膨胀跨临界CO_2循环的性能系数高约13-45%。还得出结论,随着气体冷却器温度的升高,联合热电联产循环中的纯水生产率提高。

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