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CFD Simulation of the Thermal Performance of a Parallel Counter-Parallel Flow Heat Exchanger for the Treatment of Hypothermia

机译:平行反并流式换热器热性能的CFD模拟处理低温

摘要

Hypothermia is a life-threatening condition. Currently, active warming methods are the most effective treatment for dysthermic patients. The aim of this study is to investigate the use of computational fluid dynamics (CFD) in evaluating the thermal performance of a parallel/counter-parallel flow heat exchanger used as part of a fluid warmer to treat Hypothermia. The 3D model of the heat exchanger is divided into three regions; Infusate (fluid to be heated), Hot Water (heating fluid), and a Solid Region (wall). At the end of the heat exchanger, an elbow section is used to create the counter-parallel flow arrangement specific to this design.The primary focus of this study involves evaluating heat transfer between the Infusate and Hot Water regions. Several simulations were performed for varying heat exchanger lengths (0.6, 1.2, 1.8, and 2.4m). The current CFD predicted values were compared to previously collected experimental data. In the experimental set-up, the outlet temperature was evaluated using a center-point temperature probe. The current CFD study evaluated the outlets in terms of mean bulk temperature to better characterize the thermodynamic average with respect to fluid flow. Despite this difference, the CFD results of the Infusate outlet temperatures were within 20% of the previously published experimental values. Using a center-point temperature probe, the CFD simulations were within 8% of the experimental values. It was concluded that the CFD model accurately represented the thermodynamic characteristics of the heat exchanger and can be used for future design purposes.The Hot Water region features a unique geometric variation on the traditional concentric annulus; a separation along the mid-plane confines the flow to have the area of a true concentric annulus. As such, CFD was used to investigate the thermalhydraulic effects within the Hot Water region (semi-annulus). Correlations were developed to predict the hydrodynamic and thermal developing lengths within the Hot Water region. These correlations were determined for developing flow at the inlet and after the elbow sections of the Hot Water region. CFD simulations of the Hot Water region demonstrated increasing hydrodynamic and thermal developing lengths for increasing Reynolds Number under laminar and turbulent flow. Increased mass flow rates produce increased forces within the flow area, requiring increased axial length for thermal and hydrodynamic profiles to stabilize.Developing effects within a concentric annulus has been addressed in the literature; however the flow characteristics within the proposed semi-annulus are not as well understood. A comparative study was performed evaluating the studied Hot Water semi-annulus against a true concentric annulus. The CFD developed hydrodynamic entrance length correlation for the Hot Water region (semi-annulus) under laminar flow was compared to a known entrance length correlation for a true concentric annulus. Due to the separation along the mid-plane of the Hot Water region, the flow area and wetted perimeter of a true concentric annulus is expected to be greater than that of the semi-annular geometry. Greater flow interaction with the wall in the semi-annulus increases the viscous drag on the fluid, resulting generally in a lower non-dimensionalized developing length as a function of Reynolds Number.Pressure drop within the Hot Water region was also evaluated and compared to known properties of a true concentric annulus within the fully developed region. Under both laminar and turbulent flow, the studied semi-annulus of the Hot Water region demonstrated greater pressure drop than a true concentric annulus with similar dimensions and flow conditions. The elbow section of the Hot Water region produced a significant pressure drop, which may be due to the abrupt change in flow direction resulting in increased centrifugal forces and recirculation zones.The thermal and hydrodynamic properties revealed in the CFD simulations can be used to improve future design considerations, which may lead to improved Hypothermia treatment protocols and patient care.
机译:体温过低会危及生命。当前,主动加温方法是对体温异常患者最有效的治疗方法。这项研究的目的是研究计算流体动力学(CFD)在评估作为流体加热器用于治疗体温过低的一部分的平行/逆流热交换器中的热性能。热交换器的3D模型分为三个区域:注入液(要加热的流体),热水(加热流体)和固体区域(壁)。在换热器的末端,使用弯头段来创建特定于该设计的逆平行流布置。本研究的主要重点是评估灌注液和热水区域之间的传热。针对不同的热交换器长度(0.6、1.2、1.8和2.4m)执行了一些模拟。将当前的CFD预测值与先前收集的实验数据进行比较。在实验设置中,使用中心点温度探针评估出口温度。当前的CFD研究根据平均体温对出口进行了评估,以更好地表征流体流动的热力学平均值。尽管存在这种差异,但输注液出口温度的CFD结果在先前公布的实验值的20%以内。使用中心点温度探头,CFD模拟在实验值的8%之内。结论是,CFD模型准确地代表了热交换器的热力学特性,可用于将来的设计目的。热水区域在传统的同心环上具有独特的几何变化;沿中平面的分隔将流限制为具有真正的同心环面区域。因此,CFD用于研究热水区域(半环形区域)内的热工水力效应。建立了相关性以预测热水区域内的流体动力和热力发展长度。确定了这些相关性,以便在热水区域的入口处和弯管段之后形成流动。热水区域的CFD模拟表明,在层流和湍流作用下,流体动力学和热发展长度增加,雷诺数增加。增加的质量流率会在流动区域内产生更大的力,从而需要增加轴向长度才能使热力和流体动力学轮廓稳定下来。然而,人们对所提出的半环内的流动特性的了解还不够。进行了一项比较研究,以评估研究的热水半环与一个真正的同心环。 CFD开发了层流下热水区域(半环面)的流体动力入口长度相关性,并与真实同心环面的已知入口长度相关性进行了比较。由于沿热水区域中平面的分离,真实同心环空的流动面积和润湿周长预计将大于半环形几何形状的流动面积和润湿周长。与半环形壁之间更大的流动相互作用增加了对流体的粘性阻力,通常导致较小的无量纲的显影长度(作为雷诺数的函数)。还对热水区域内的压降进行了评估并与已知的进行了比较完全发达区域内真正同心环的性质。在层流和湍流下,所研究的热水区域的半环空均比具有相似尺寸和流动条件的真实同心环空具有更大的压降。热水区域的弯头部分产生了明显的压降,这可能是由于流动方向的突然变化导致离心力和再循环区域增加所致.CFD模拟中显示的热力学和流体力学特性可用于改善未来设计方面的考虑,这可能会导致改善低温治疗方案和患者护理。

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    Heller Alex;

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  • 年度 2014
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