首页> 外文期刊>Journal of Food Science and Technology >Influence of particle-particle, interactions of fluid-to-particle heattransfer coefficients (h(fp)) under tube flow conditions using stationaryparticle technique
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Influence of particle-particle, interactions of fluid-to-particle heattransfer coefficients (h(fp)) under tube flow conditions using stationaryparticle technique

机译:使用固定颗粒技术在管流条件下颗粒间的影响,流体间的传热系数(h(fp))的相互作用

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Fluid-to-particle heat transfer coefficients (h(fp)) were determined experimentally during flow of fluid over one or more particles using "stationary particle technique". The effects of different process parameters (e.g., particle-particle interaction, carrier fluid viscosity, carrier fluid temperature and flow rate) on h(fp) were quantified. The h(fp) value for the sample particle (silicone sphere) decreased by 5-20%, when another particle at different orientations (0 degrees, 30 degrees, 45 degrees and 60 degrees) was introduced upstream, whereas h(fp) values increased by 14%, when multiple particles were introduced upstream of the sample particle (flow rate = 5.2 x 10(-4)m(3)/s and fluid temperature = 73.6 degreesC). The h(fp) value decreased three-folds with an increase in carrier fluid viscosity from 0.4 x 10(-3) to 33.3 x 10(-3) Pa.s. The h(fp) values increased four- and two-folds with an increase in carrier fluid temperature (from 60 degrees to 80 degrees) and flow rate (from 0.27 10(-3) to 2.82 x 10(-3)m(3)/s), respectively.
机译:使用“固定粒子技术”,在流体流过一个或多个粒子的过程中,实验确定了粒子间的传热系数(h(fp))。量化了不同工艺参数(例如,颗粒-颗粒相互作用,载体流体粘度,载体流体温度和流速)对h(fp)的影响。当另一个不同方向(0度,30度,45度和60度)的粒子被引入上游时,样品粒子(硅球)的h(fp)值降低了5-20%,而h(fp)值当在样品颗粒的上游引入多个颗粒时(流速= 5.2 x 10(-4)m(3)/ s,流体温度= 73.6摄氏度),流速增加了14%。 h(fp)值随载液粘度从0.4 x 10(-3)Pa.s增加到33.3 x 10(-3)Pa.s下降了三倍。 h(fp)值随着载液温度(从60度到80度)和流速(从0.27 10(-3)到2.82 x 10(-3)m(3)的增加而增加了四倍和两倍。 )/ s)。

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