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Estimation of diffusion parameters in fluidized bed drying

机译:流化床干燥中扩散参数的估计

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摘要

The present work is an attempt to assess the drying kinetics of green pepper in a fluidized bed in a temperature range of 65-105 °C. The drying kinetics is modeled using several semi empirical models to estimate the kinetic parameters. Although the semi empirical model could fit the experimental data well within acceptable experimental error limits, the two parameter models such as Henderson Pabis model and Page Model are identified to predict the drying kinetics with lesser error. The kinetic parameter (k) is found to increase with the temperature for all the models. The activation energy (E) estimated using Arrhenius equation is found to be 30.3 kJ/mol, while the Arrhenius constant (k_o) is found to be 0.09 s~(-1). The effective diffusivity coefficient is evaluated using Fick's diffusion equation which is found increase with increase in temperature of the heating medium and to vary from 1.95 x 10~(-11) to 7 x 10~(-11) m2/s.
机译:目前的工作是尝试评估青椒在65-105°C温度范围内在流化床中的干燥动力学。使用几个半经验模型对干燥动力学进行建模,以估算动力学参数。尽管半经验模型可以在可接受的实验误差范围内很好地拟合实验数据,但仍可以识别两个参数模型(例如,亨德森·帕比斯模型和佩奇模型),以预测误差较小的干燥动力学。对于所有模型,动力学参数(k)随温度增加而增加。发现使用Arrhenius方程估算的活化能(E)为30.3 kJ / mol,而Arrhenius常数(k_o)为0.09 s〜(-1)。使用Fick扩散方程评估有效扩散系数,该方程随加热介质温度的升高而增加,范围从1.95 x 10〜(-11)到7 x 10〜(-11)m2 / s。

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