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An empirical methodology for evaluating the fluid to particle heat transfer coefficient in bi-axially rotating cans using liquid temperature data.

机译:一种使用液体温度数据评估双轴旋转罐中流体与颗粒之间的传热系数的经验方法。

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摘要

An empirical methodology was developed for evaluating the fluid to particle heat transfer coefficient (hfp) and overall heat transfer coefficient (U) in bi-axially rotating cans. Conventional particle temperature measurement during thermal processing is generally difficult in cans undergoing agitation processing and is even more difficult in cans going through bi-axial free rotation as in continuous flow turbo cookers. Thin wire flexible thermocouples have helped in gathering temperature data of both particle and liquid in end-over-end batch processes. Wireless temperature loggers have been developed for liquid temperature measurements in continuous flow systems which can be used to estimate U. Evaluation of hfp is still difficult in these systems due to difficulty in gathering particle temperatures. The proposed method involves developing correlations between hfp and U using real time-temperature data gathered from test cans in fixed axial mode and then coupling them with experimentally evaluated U from fluid temperature gathered with wireless sensors to compute hfp for bi-axially rotating cans. The methodology is based on the assumption that within a can, factors that influence U will also influence hfp, and therefore hfp and U are generally interrelated. A three factor, five level central composite rotatatable design and a response surface methodology was used to develop the correlation models for the U and hfp in fixed axial mode with retort temperature (111.6-128.4 degrees C), glycerin concentration (80-100%), and rotational speed (4-24 rpm) as the main factors. The developed model was used to evaluate the U and hfp in the free bi-axial mode, using a full factorial design (3x3 factorial). The method was successfully implemented and an analysis of variance study, as expected, indicated all three major factors to influence the U and hfp values. Glycerin concentration and rotation speed were highly significant (<0.001), while temperature was marginally significant (p<0.05) with respect to U while all factors were significant with hfp.
机译:开发了一种经验方法来评估流体在颗粒间的传热系数( h fp )和总传热系数( U )。轴向旋转的罐头。在热处理过程中,常规的颗粒温度测量通常在经受搅拌处理的罐中是困难的,并且如在连续流涡轮炊具中那样,在经历双轴自由旋转的罐中甚至更加困难。细线柔性热电偶有助于在端到端批处理过程中收集颗粒和液体的温度数据。开发了无线温度记录器,用于连续流系统中的液体温度测量,可用于估算 U 。由于难以收集粒子温度,因此在这些系统中仍然很难评估 h fp 。所提出的方法涉及使用从固定轴模式下的测试罐收集的实时温度数据来开发 h fp 和 U 之间的相关性,然后将它们耦合用无线传感器收集的流体温度对 U 进行实验评估,以计算双轴旋转罐的 h fp 。该方法基于以下假设:在罐中,影响 U 的因素也将影响 h fp ,因此也会影响 h < / i> fp 和 U 通常是相互关联的。使用三因素,五层中央复合材料可旋转设计和响应面方法开发了 U 和 h fp 的相关模型以干馏温度(111.6-128.4摄氏度),甘油浓度(80-100%)和转速(4-24 rpm)为主要因素的固定轴向模式。使用完整的因子设计(3x3因子),使用开发的模型以自由双轴模式评估 U 和 h fp 。该方法已成功实施,并且按预期进行的方差分析表明,所有三个主要因素都会影响 U 和 h fp 值。甘油的浓度和旋转速度与 U 高度相关(<0.001),而温度仅与之相关( p <0.05),而所有因素对 h fp

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