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ESTIMATION OF CONVECTIVE HEAT TRANSFER BETWEEN FLUID AND PARTICLE IN CONTINUOUS FLOW USING A REMOTE TEMPERATURE SENSOR

机译:使用远程温度传感器估算连续流动中流体与颗粒之间的对流换热

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摘要

The convective heat transfer coefficient (h_(fp)) between fluid and particle in continuous tube flow was estimated using a temperature pill, a remote electronic temperature sensor which uses a quartz crystal as the temperature sensing element. The temperature history of a particle (with temperature pill mounted within) was monitored as it moved through a test section. A finite element algorithm was then used to back calculate h_(fp) from the time-temperature data. The value of h_(fp) ranged from 134 W/m~2K to 669 W/m~2K (Nu=3.6 to 17.3) over a fluid generalized Reynolds number range (restricted by experimental constraints) from 19 to 196.8. As expected, h_(fp) decreased with increasing carrier medium viscosity and increased with increasing flow rates. Even with several conservative factors at play, the lowest Nusselt number was greater than the 2.0 expected for a spherical panicle in a stagnant fluid. Potential applications of the technique include noninvasive measurement of the temperature (and h_(fp) values) of the panicles moving within a fluid stream in otherwise inaccessible locations.
机译:连续管流动中流体与颗粒之间的对流传热系数(h_(fp))是使用温度药丸估算的,该药丸是使用石英晶体作为温度感应元件的远程电子温度传感器。当颗粒(通过温度丸安装在其中)通过测试部分时,对其温度历史进行监控。然后使用有限元算法根据时间-温度数据反算h_(fp)。在从19到196.8的流体广义雷诺数范围内(受实验约束限制),h_(fp)的值范围从134 W / m〜2K到669 W / m〜2K(Nu = 3.6到17.3)。如预期的那样,h_(fp)随着载体介质粘度的增加而降低,并随着流速的增加而增加。即使有几个保守因素起作用,最低的Nusselt值仍大于停滞液中球形圆锥花序的2.0。该技术的潜在应用包括无创测量在流体流中在其他无法到达的位置移动的穗的温度(和h_(fp)值)。

著录项

  • 来源
    《Journal of food process engineering》 |1996年第2期|p.223-240|共18页
  • 作者单位

    The National Center for Food Safety and Technology, Illinois Institute of Technology, Summit-Argo, IL 60501;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 食品工业;
  • 关键词

  • 入库时间 2022-08-17 23:25:28

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