Effect of an Internal Heat Exchanger on the Performances of a Double Evaporator Ejector Refrigeration Cycle

A theoretical investigation is presented about a double evaporator ejector refrigeration cycle(DEERC).Special attention is paid to take into account the influence of the sub-cooling and superheating effects induced by an internal heat exchanger(IHX).The ejector is introduced into the baseline cycle in order to mitigate the throttling process losses and increase the compressor suction pressure.Moreover,the IHX has the structure of a concentric counter-flow type heat exchanger and is intentionally used to ensure that the fluid at the compressor inlet is vapor.To assess accurately the influence of the IHX on the DEERC performance,a mathematical model is derived in the frame of the dominant one-dimensional theory for ejectors.The model also accounts for the friction effect in the ejector mixing section.The equations of this model are solved using an Engineering Equation Solver(EES)for different fluids.These are:R134a as baseline fluid and other environment friendly refrigerants used for comparison,namely,R1234yf,R1234ze,R600,R600a,R290,R717 and R1270.The simulation results show that the DEERC with an IHX can achieve COP(the coefficient of performance)improvements from 5.2 until 10%.

太阳能压缩-喷射二级制冷系统的运行工况分析

压缩-喷射二级制冷系统的COP较传统的喷射制冷系统的COP提高了20%～50%。本文分析了发生温度、中间温度、冷凝温度、蒸发温度对以太阳能为热源的压缩-喷射二级制冷系统的运行工况的影响。结果表明,在综合考虑技术和经济的前提下,应尽可能地提高系统运行的发生温度,降低冷凝温度,中间温度的选择应兼顾集热器的面积和系统的性能系数。

满液式蒸发器用孔板膨胀节流装置的设计与Excel的自动计算方法

就满液式蒸发器用膨胀节流装置—孔板的设计方法进行阐述,以林宗虎算式作为理论基础,详细说明如何利用Excel VBA制作专门的自动计算软件。实践证明,该孔板设计方法可以很好地满足螺杆式冷水机组/离心式冷水机组的使用要求,该软件可以准确计算孔板的孔数及液管的管径等设计参数,对设计开发工作很有帮助。

新型双蒸发制冷系统制冷剂的研究

研究了喷射器内部流体流动过程,应用质量守恒、动量守恒、能量守恒对两相喷射器建立了热力学模型,分析了不同制冷剂对新型双蒸发制冷系统性能的影响。计算结果表明:新型双蒸发系统中,当蒸发和冷凝温度相同时,R152a的性能系数高于其他4种制冷剂,R143a的喷射系数、喷射器的压缩效率、制冷量和性能系数提高率均高于其他4种制冷剂;当蒸发温度不变时,性能系数提高率随着冷凝温度的升高而降低,冷凝温度为30℃时,制冷剂为R143a,性能系数提高率达20%。

新型双蒸发两级压缩/喷射制冷系统性能分析

为提高两级压缩制冷系统性能,提出了一种新型双蒸发两级压缩/喷射制冷系统,建立了系统热力学计算模型,对不同工况下的系统性能进行了研究。结果表明:当低温蒸发器和高温蒸发器的蒸发温度升高时,新系统性能系数和单位容积制冷量都增大;当冷凝温度升高时,性能系数、制冷量和相对于传统系统的性能系数提升率都减小;当蒸发和冷凝温度固定时,随着中间温度的升高,性能系数先增大后减小。在低温蒸发器和高温蒸发器的蒸发温度分别为-10℃和0℃、冷凝温度为40℃的情况下,当中间温度为20℃时,性能系数达到最大值4.7,与传统系统相比新系统性能系数提升率均在17%以上。