{"title":"Experimental investigation of Multi-Mode heat transfer to a Free-Falling dilute particle cloud in a heated vertical tube","authors":"Muhammad Umer, Bryan J. Siefering, Brian M. Fronk","doi":"10.1016/j.expthermflusci.2024.111278","DOIUrl":null,"url":null,"abstract":"<div><p>The development of dilute particle heat exchangers and reactors for advanced energy systems requires an understanding of the multi-mode heat transfer from a heated wall to falling particles. This study presents experimental results of the overall heat transfer coefficient for a free-falling, dilute flow of particles with solid volume fraction from 0.0005 to 0.006 corresponding to feed rates from 3.7 kg s<sup>−1</sup> m<sup>−2</sup> to 44 kg s<sup>−1</sup> m<sup>−2</sup> in a vertical, heated tube containing quiescent air at atmospheric pressure. Tube wall temperatures are varied between 300°C to 900°C while keeping the particle inlet temperature constant. The experimental results show that the overall heat transfer coefficient is a strong function of particle feed rate and surface temperature. Good agreement was obtained with prior studies conducted at comparable temperatures but lower particle feed rates (<4 kg m<sup>−2</sup> s<sup>−1</sup>). The established correlations for particle-to-wall radiation and particle-to-gas convection were used to estimate the wall-to-gas convective contribution from the measured overall heat transfer coefficient. The experimental results indicated a 4 to 6 times improvement in the wall convection in the solid–gas mixture compared to that expected from natural convection in a single-phase gas. The data presented here are applicable to characterize heat transfer in dilute particle heat exchangers, furnaces, and solar receivers.</p></div>","PeriodicalId":12294,"journal":{"name":"Experimental Thermal and Fluid Science","volume":"159 ","pages":"Article 111278"},"PeriodicalIF":2.8000,"publicationDate":"2024-08-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Experimental Thermal and Fluid Science","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S089417772400147X","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, MECHANICAL","Score":null,"Total":0}
引用次数: 0
Abstract
The development of dilute particle heat exchangers and reactors for advanced energy systems requires an understanding of the multi-mode heat transfer from a heated wall to falling particles. This study presents experimental results of the overall heat transfer coefficient for a free-falling, dilute flow of particles with solid volume fraction from 0.0005 to 0.006 corresponding to feed rates from 3.7 kg s−1 m−2 to 44 kg s−1 m−2 in a vertical, heated tube containing quiescent air at atmospheric pressure. Tube wall temperatures are varied between 300°C to 900°C while keeping the particle inlet temperature constant. The experimental results show that the overall heat transfer coefficient is a strong function of particle feed rate and surface temperature. Good agreement was obtained with prior studies conducted at comparable temperatures but lower particle feed rates (<4 kg m−2 s−1). The established correlations for particle-to-wall radiation and particle-to-gas convection were used to estimate the wall-to-gas convective contribution from the measured overall heat transfer coefficient. The experimental results indicated a 4 to 6 times improvement in the wall convection in the solid–gas mixture compared to that expected from natural convection in a single-phase gas. The data presented here are applicable to characterize heat transfer in dilute particle heat exchangers, furnaces, and solar receivers.
开发用于先进能源系统的稀颗粒热交换器和反应器需要了解从加热壁到下落颗粒的多模式传热。本研究介绍了自由下落的稀颗粒流的总体传热系数的实验结果,这些颗粒的固体体积分数从 0.0005 到 0.006 不等,进料速率从 3.7 kg s m 到 44 kg s m 不等。管壁温度在 300°C 至 900°C 之间变化,而颗粒入口温度保持不变。实验结果表明,总体传热系数是颗粒进料速率和表面温度的一个重要函数。这与之前在温度相当但颗粒进料速率较低(<4 kg m s)的条件下进行的研究结果十分吻合。利用已建立的颗粒对壁辐射和颗粒对气体对流的相关性,可以从测量的整体传热系数中估算出壁对气体对流的贡献。实验结果表明,与单相气体中的自然对流相比,固气混合物中的壁面对流提高了 4 到 6 倍。本文提供的数据适用于描述稀颗粒热交换器、熔炉和太阳能接收器的传热特性。
期刊介绍:
Experimental Thermal and Fluid Science provides a forum for research emphasizing experimental work that enhances fundamental understanding of heat transfer, thermodynamics, and fluid mechanics. In addition to the principal areas of research, the journal covers research results in related fields, including combined heat and mass transfer, flows with phase transition, micro- and nano-scale systems, multiphase flow, combustion, radiative transfer, porous media, cryogenics, turbulence, and novel experimental techniques.