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Simulation Research of Heat Transfer Characteristics of Carbon Dioxide in Microchannel Evaporator

机译:微通道蒸发器中二氧化碳传热特性的仿真研究

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摘要

In this paper, the simulation model of two-dimensional (2D) distribution parameter of a CO2 microchannel evaporator was developed using the finite element method. The simulation model of the CO2 microchannel evaporator was written using MATLAB both considering the dry and wet conditions on air side, and different heat transfer characteristics of CO2 in two-phase region and overheated region. The experimental and simulation results in terms of CO2 temperature, wall temperature, inlet and outlet air temperatures, and convective heat transfer coefficient were compared. The simulation results have the same tendency with the experimental correlation results. The convective heat transfer efficient increases with the growth of CO2 inlet dryness, mass flow rate and air speed, while decreases along with the increase of evaporation pressure in two-phase region. The dry-out point appears earlier with larger CO2 inlet dryness, and higher air temperature, humidity and speed; however, it appears later with the increasing evaporation pressure and mass flow rate. The convective heat transfer coefficient at the dry-out point decreases dramatically due to the deteriorated heat transfer at this position, which indicates the necessity to prevent or retard the appearance of dry-out point.
机译:本文采用有限元法开发了CO2微通道蒸发器二维(2D)分布参数的仿真模型。 CO2微通道蒸发器的模拟模型使用MATLAB考虑空气侧的干燥和湿条件,以及两相区域中CO 2的不同传热特性和过热区域。比较了CO 2温度,壁温,入口和出口空气温度和对流传热系数的实验和仿真结果。仿真结果具有与实验相关结果相同的趋势。随着二氧化碳入口干燥,质量流速和空气速度的生长,对流传热有效地增加,而两相区域中的蒸发压力的增加随着蒸发压力的增加而降低。干出点早先出现,具有较大的CO 2入口干燥,以及更高的空气温度,湿度和速度;然而,随后似乎越来越大的蒸发压力和质量流量。由于在该位置处的热传递劣化,干出点的对流传热系数在显着降低,这表明必须预防或延迟干燥点的外观。

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