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超临界二氧化碳在高质量通量垂直向上管内流动传热特性的数值研究

Numerical Investigation of Heat Transfer Characteristics of scCO Flowing in a Vertically-Upward Tube with High Mass Flux.

作者信息

Gong Kaigang, Zhu Bingguo, Peng Bin, He Jixiang

机构信息

School of Mechanical & Electronical Engineering, Lanzhou University of Technology, Lanzhou 730050, China.

出版信息

Entropy (Basel). 2022 Jan 1;24(1):79. doi: 10.3390/e24010079.

Abstract

In this work, the heat transfer characteristics of supercritical pressure CO in vertical heating tube with 10 mm inner diameter under high mass flux were investigated by using an SST - turbulent model. The influences of inlet temperature, heat flux, mass flux, buoyancy and flow acceleration on the heat transfer of supercritical pressure CO were discussed. Our results show that the buoyancy and flow acceleration effect based on single phase fluid assumption fail to explain the current simulation results. Here, supercritical pseudo-boiling theory is introduced to deal with heat transfer of scCO. scCO is treated to have a heterogeneous structure consisting of vapor-like fluid and liquid-like fluid. A physical model of scCO heat transfer in vertical heating tube was established containing a gas-like layer near the wall and a liquid-like fluid layer. Detailed distribution of thermophysical properties and turbulence in radial direction show that scCO heat transfer is greatly affected by the thickness of gas-like film, thermal properties of gas-like film and turbulent kinetic energy in the near-wall region. Buoyancy parameters < 10, < 5.6 × 10 and flow acceleration parameter < 3 × 10 in this paper, which indicate that buoyancy effect and flow acceleration effect has no influence on heat transfer of scCO under high mass fluxes. This work successfully explains the heat transfer mechanism of supercritical fluid under high mass flux.

摘要

在这项工作中,采用SST湍流模型研究了内径为10mm的垂直加热管内超临界压力CO在高质量通量下的传热特性。讨论了入口温度、热通量、质量通量、浮力和流动加速度对超临界压力CO传热的影响。我们的结果表明,基于单相流体假设的浮力和流动加速度效应无法解释当前的模拟结果。在此,引入超临界拟沸腾理论来处理超临界CO2的传热问题。超临界CO2被视为具有由汽态流体和液态流体组成的非均匀结构。建立了垂直加热管内超临界CO2传热的物理模型,该模型包含靠近管壁的气态层和液态流体层。热物理性质和湍流在径向上的详细分布表明,超临界CO2的传热受气态膜厚度、气态膜热性质和近壁区域湍动能的显著影响。本文中浮力参数<10、<5.6×10,流动加速度参数<3×10,这表明在高质量通量下,浮力效应和流动加速度效应对超临界CO2的传热没有影响。这项工作成功地解释了高质量通量下超临界流体的传热机理。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/b51c/8774452/817802739afe/entropy-24-00079-g001.jpg

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