受底部加热的近临界流体室热响应的定量测量

IF 2.6 3区 工程技术 Q2 ENGINEERING, MECHANICAL
Rui Zhang , Yizhi Zhang , Jinliang Xu , Lin Chen
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引用次数: 0

摘要

超临界CO2在工业中的广泛应用,需要理解非线性、非单调行为的热物理性质与接近临界点或伪临界线区域的基本传热过程之间的耦合机制。本文以近临界对流为研究对象(rayleigh - b海姆纳德模型),研究了近临界对流的不稳定性及其流型与换热特性的相关性。采用改进的移相干涉仪捕获瞬态密度和温度场数据,便于对局部流体行为的研究。测量是在接近临界点的几个特定工况下进行的,也沿着伪临界线(初始条件Ti = 32.00 ~ 36.00℃,pi = 7.50 ~ 8.30 MPa),不同的热通量q = 164、657和1477 W/m2。主要研究结果包括:(1)总体上观测到对流和羽流,温度变化在10 ~ 60 mK之间,Nusselt数在7 mm长度尺度上可达8 × 104;(2)在相同加热条件下,类气情况下对流触发更快主要是由于动力黏度小,而热边界层在拟临界线或临界点附近的热膨胀系数βp增大是导致热边界层不稳定的原因;(3) Nusselt数的不均匀分布表明存在小羽流(在长度尺度上约为1 mm, Nusselt数变化为2 × 103),这表明在小尺度上传热强度不均匀。在接近临界点或拟临界线时,这种现象更为重要,这也说明了对流换热局部效应在超临界流体系统设计和运行中的重要性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Quantitative measurement of thermal responses of a near-critical fluid chamber subjected to bottom heating
A broader application of supercritical CO2 in the industry has invoked the need for the understanding of the coupling mechanism between the non-linear, non-monotonous behaving thermophysical properties with the fundamental heat transfer process in the region close to the critical point or the pseudo-critical line. In this research, a near-critical convective flow when subjected to the heat from the bottom (Rayleigh–Bénard model) is studied to investigate its instability and correlation behavior between the flow pattern and heat transfer characteristic. An improved phase-shifting interferometer is applied to capture transient density and temperature field data, facilitating the investigation of local fluid behavior. The measurement is conducted under several specific working conditions close to the critical point and also along the pseudo-critical line (initial conditions Ti = 32.00 ∼ 36.00 ℃, pi = 7.50 ∼ 8.30 MPa), and under different heat fluxes q = 164, 657, and 1477 W/m2. The main findings include: (1) In general, the convection and the plume flow are observed with the temperature changes of 10 ∼ 60 mK and Nusselt number up to 8 × 104 in the length scale of 7 mm; (2) The faster trigger of convective flow under the same heating conditions in the gas-like cases is mainly due to the small dynamic viscosity, while the enlarged thermal expansion coefficient βp near the pseudo-critical line or the critical point is responsible for the instability of the thermal boundary layer; (3) The inhomogeneous distribution of Nusselt number indicates the existence of small plume flow (on the length scale about 1 mm with variation in Nusselt number of 2 × 103), which shows an inhomogeneous transfer heat transfer intensity in a small scale. This phenomenon is more important when the critical point or the pseudo-critical line is approached, which also indicates the importance of the local effect of convective heat transfer in the design and operation of the supercritical fluids system.
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来源期刊
International Journal of Heat and Fluid Flow
International Journal of Heat and Fluid Flow 工程技术-工程:机械
CiteScore
5.00
自引率
7.70%
发文量
131
审稿时长
33 days
期刊介绍: The International Journal of Heat and Fluid Flow welcomes high-quality original contributions on experimental, computational, and physical aspects of convective heat transfer and fluid dynamics relevant to engineering or the environment, including multiphase and microscale flows. Papers reporting the application of these disciplines to design and development, with emphasis on new technological fields, are also welcomed. Some of these new fields include microscale electronic and mechanical systems; medical and biological systems; and thermal and flow control in both the internal and external environment.
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