{"title":"UNSTEADY NUMERICAL SIMULATION OF DYNAMIC REACTOR - EVAPORATOR INTERACTION IN THERMOCHEMICAL REFRIGERATION SYSTEMS","authors":"J. Mejía, F. Chejne, F. Cortés","doi":"10.29047/01225383.51","DOIUrl":null,"url":null,"abstract":"Close interaction between evaporation/reaction rates in gas-solid refrigeration cycles promotes the \ndynamic behavior of gas pressure in gas-liquid and gas-solid interfaces in evaporators and reactor \ndiffusers. Simultaneously, gas pressure modifies both reaction rates in reactors and mass and energy \ntransfer rates in reactors and evaporators. The objective of this work is to model the complex interaction between \nreactor and evaporator using a phenomenological approach. The coupled interaction is studied by a \nnovel mathematical model of the reactor and evaporator at the synthesis/evaporation step. The model of the \ngas-solid reactor is based on unsteady 2-D mass, momentum and energy transport equations. The evaporator \nmodel considers the interaction between evaporation/reaction rates given by the unsteady mass and \nenergy transfer at heterogeneous interfaces and with other components. The thermodynamic properties of the \nrefrigerant are calculated by the Patel-Teja equation-of-state. Simulation results predicted by the model were \nsatisfactorily validated with experimental data. Predicted interaction between reactor, evaporator and cooling \nspace showed non-linear behavior of gas pressure. The simulation results showed that, if the dynamics of the \nevaporator and cooling space are neglected, coefficient of performance (COP) is overestimated by 32% for \nthe configuration evaluated in this work.","PeriodicalId":10235,"journal":{"name":"Ciencia Tecnologia y Futuro","volume":"11 1","pages":"107-126"},"PeriodicalIF":0.0000,"publicationDate":"2013-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Ciencia Tecnologia y Futuro","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.29047/01225383.51","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
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.