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Numerical Simulation on Flow and Heat Transfer Characteristics of Supercritical Fluids in Mini-Channels

机译:超临界流体在微通道中流动和传热特性的数值模拟

摘要

This paper investigated the flow and heat transfer characteristics of supercritical carbon dioxide (SC-CO2) and supercritical water (SC-H2O) in horizontal micro-channels using a CFD approach. Model of a straight circular pipe of stainless steel with internal and external radii of , respectively, and a heated length of 55 mm was considered. For the simulation, carbon dioxide and water at supercritical pressures of 9.5 MPa and 22.07 MPa respectively were used, while uniform heat was applied on the outer surface of the tube. The thermodynamics properties for both fluids were obtained from the NIST Chemistry Web book. The simulated temperature and heat transfer coefficient variation were compared with experimental results from literature. In general, the simulation results were close to the experiment. Both the simulation and experimental results showed that the wall temperature increased along the tube length. As expected, the heat transfer coefficient values for both supercritical fluids decreased as the length of the tube. This was due the reason that a maximum and dominant convection heat transfer occurred at the entrance of the heated section of the pipe. The results from this study could assist in decisions regarding the use of supercritical fluids in industries which involve heat transfer.ud
机译:本文利用CFD方法研究了水平微通道中超临界二氧化碳(SC-CO2)和超临界水(SC-H2O)的流动和传热特性。考虑了一个直的圆形不锈钢管的模型,该管的内部和外部半径分别为,加热长度为55 mm。为了进行模拟,分别使用了超临界压力为9.5 MPa和22.07 MPa的二氧化碳和水,同时在管的外表面施加了均匀的热量。两种流体的热力学性质可从NIST Chemistry Web书中获得。将模拟的温度和传热系数变化与文献中的实验结果进行了比较。通常,模拟结果接近于实验。仿真和实验结果均表明,壁温沿管长增加。正如预期的那样,两种超临界流体的传热系数值都随着管的长度而减小。这是由于在管道的受热部分的入口处发生最大的对流传热的原因。这项研究的结果可能有助于做出有关超临界流体在涉及传热的行业中使用的决策。 ud

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