热化学制冷系统中反应器-蒸发器相互作用的非定常数值模拟

J. Mejía, F. Chejne, F. Cortés
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引用次数: 0

摘要

在气固制冷循环中,蒸发/反应速率之间的密切相互作用促进了蒸发器和反应器扩散器中气液和气固界面气体压力的动态行为。同时,气体压力改变反应器中的反应速率以及反应器和蒸发器中的质量和能量传递速率。这项工作的目的是用现象学的方法来模拟反应器和蒸发器之间复杂的相互作用。通过建立反应器和蒸发器在合成/蒸发阶段的数学模型,研究了两者之间的耦合作用。气固反应器模型基于非定常二维质量、动量和能量输运方程。蒸发器模型考虑了非定常质量和能量传递所给出的蒸发/反应速率与其他组分之间的相互作用。制冷剂的热力学性质由Patel-Teja状态方程计算。模型预测的仿真结果与实验数据得到了满意的验证。预测的反应器、蒸发器和冷却空间之间的相互作用表现出气体压力的非线性行为。仿真结果表明,如果忽略蒸发器和冷却空间的动力学,本研究评估的配置的性能系数(COP)高估了32%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
UNSTEADY NUMERICAL SIMULATION OF DYNAMIC REACTOR - EVAPORATOR INTERACTION IN THERMOCHEMICAL REFRIGERATION SYSTEMS
Close interaction between evaporation/reaction rates in gas-solid refrigeration cycles promotes the dynamic behavior of gas pressure in gas-liquid and gas-solid interfaces in evaporators and reactor diffusers. Simultaneously, gas pressure modifies both reaction rates in reactors and mass and energy transfer rates in reactors and evaporators. The objective of this work is to model the complex interaction between reactor and evaporator using a phenomenological approach. The coupled interaction is studied by a novel mathematical model of the reactor and evaporator at the synthesis/evaporation step. The model of the gas-solid reactor is based on unsteady 2-D mass, momentum and energy transport equations. The evaporator model considers the interaction between evaporation/reaction rates given by the unsteady mass and energy transfer at heterogeneous interfaces and with other components. The thermodynamic properties of the refrigerant are calculated by the Patel-Teja equation-of-state. Simulation results predicted by the model were satisfactorily validated with experimental data. Predicted interaction between reactor, evaporator and cooling space showed non-linear behavior of gas pressure. The simulation results showed that, if the dynamics of the evaporator and cooling space are neglected, coefficient of performance (COP) is overestimated by 32% for the configuration evaluated in this work.
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