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超临界流体广泛应用于工程技术领域, 其流动传热特性对工程设计具有重要意义, 但是, 由于超临界流体的物理微观和宏观行为的机理尚不清晰, 所以其异常的流动传热特性并未得到很好的解决. 普遍认为超临界流体在分子尺度上可分为类气和类液两种不同的特性, 直到最近通过实验在宏观上监测到超临界水类液和类气之间的转变, 且这一过程与拟沸腾理论一致, 使得问题逐渐变得清晰. 本文基于拟沸腾理论对超临界CO 2异常流动传热行为进行了研究, 在假设类液和类气转换过程不均匀的情况下, 从经典的量纲分析和亚临界过冷沸腾理论模型出发, 提出了一个适用于超临界流体拟沸腾换热过程的分析方法. 通过引入表征类气膜生长速度与流体主流平均流速之比 π= ( q w· ρ l)/( G·Δ i· ρ g)和表征近壁区类气膜温度梯度 π 13= ( q w· β pc· d i)/ λ g两个无量纲数, 来表征拟沸腾如何导致传热恶化, 解释了超临界CO 2竖直向上加热流动过程中的异常换热特性, 即较大的类气膜生长速度使近壁区快速聚集了较多的高温流体, 而较大的类气膜温度梯度使类气膜覆盖在壁面. 当核心的冷类液不能充分润湿热壁面时, 传热恶化. 新无量纲数较好的诠释了超临界流体拟沸腾诱导传热恶化机制, 为超临界拟沸腾传热研究提供了理论依据.Supercritical fluids are widely used in engineering technology, and the flow and heat transfer characteristics are very important for engineering design. However, due to the fact that the physical micro- and macroscopic behaviors of supercritical fluids are still open, neither the heat transfer mechanism nor the flow mechanism of supercritical fluids has been well revealed. It is widely believed that liquid-like (LL) and gas-like (GL) supercritical fluid are two phases distinguishable on a molecular scale. Only recently, has it become clear that the macroscopic transition from LL to GL supercritical state, when crossing the Widomline, is successfully detected in experiment, and explained based on the pseudo-boiling concept. In this paper, the abnormal flow and heat transfer behavior of supercritical CO 2are studied based on the pseudo-boiling theory. On the assumption that the transition from LL to GL is heterogeneous, an analysis method for pseudo-boiling heat transfer is developed from classical dimensional analysis and subcritical subcooled boiling theory of models. To analyze the pseudo-boiling resulting in heat transfer deterioration process of supercritical fluid, two dimensionless numbers which are π= ( q w· ρ l)/( G·Δ i· ρ g) and π 13= ( q w· β pc· d i)/ λ gare proposed to explain the anomalous heat transfer characteristics in vertical upward heating flow. The former πreflects the rate of conversion between gas-like and liquid-like fluid. The larger gas-like conversion rate promotes the rapid production of more high-temperature fluid in the near-wall region, and the latter π 13characterizes the temperature gradient of gas-like film near the wall: the larger temperature gradient causes the gas film to cover the wall surface. The heat transfer deterioration may occur when the cooler liquid-like fluid of the core region cannot rewet the hot wall adequately. The new dimensionless numbers can successfully explain the heat transfer deterioration of supercritical fluid flow induced by pseudo-boiling. Our work paves the way to understanding the heat transfer and flow for supercritical fluids which establishes a relation among the internal flow, heat transfer field characteristics, boundary conditions and physical properties based on the pseudo-boiling theory preliminarily. The results of dimensional analysis can be applied to the similarity theory analysis of different fluids, which is of significance for promoting the theoretical research of supercritical fluid heat transfer on the basis of pseudo-boiling concept.
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Keywords:
- supercritical carbon dioxide/
- pseudo-boiling/
- heat transfer deterioration/
- dimensional analysis
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