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首页> 外文期刊>Drying technology: An International Journal >Mathematical Model of Fixed-Bed Drying and Strategies for Crumb Rubber Producing STR20
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Mathematical Model of Fixed-Bed Drying and Strategies for Crumb Rubber Producing STR20

机译:固定胶干燥的数学模型及生产STR20的生胶的策略

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摘要

The objectives of this research were to investigate empirical and diffusion models for thin-layer crumb rubber drying for producing STR20 rubber using hot air temperatures of 110-130°C and to study the effect of drying parameters such as inlet drying temperature, volumetric flow rate, and initial moisture content on the quality of dried rubber. Finally, a mathematical drying model for predicting the drying kinetics of crumb rubber was developed using inlet air flow rates of 300-600 m~3/min-m~3 of crumb rubber (equivalent to 1.8-5.0 m/s) with the crumb rubber thickness fixed at 0.25 m. The average initial moisture content of samples was in the ranges of 40 and 50% dry basis while the desired final moisture content was below 5% dry basis. The results showed that the drying equation of crumb rubber was highly related to the inlet air temperature, while the drying constant value was not proportional to the initial moisture content. Consequently, the experimental data were formulated using nine empirical models and the analytical solution of moisture ratio equation was developed by Fick's law of diffusion. The result showed that the simulated data best fitted the logarithmic model and was in reasonable agreement to the experimental data. The effective diffusion coefficient of crumb rubber was in the range of 1.0 x 10~(-9) to 2.15 x 10~(-5)m~2/s corresponding to drying temperatures between 40 and 150°C, respectively. The effects of air recirculation, inlet drying temperature, initial moisture contents, air flow rate, and drying strategies on specific energy consumption and quality of samples were reported. The experiments were conducted using two different drying strategies as follows: one-stage and two-stage drying conditions. The results showed that initial moisture content and air flow rates significantly affected the specific energy consumption and quality of rubber, while the volumetric air flow rate acted as dominant effect to the specific energy consumption. The simulated results concluded that the percentage of recycled air between 90 and 95% provided the lowest specific energy consumption as compared to the others.
机译:这项研究的目的是研究使用110-130°C的热空气温度生产STR20橡胶的薄层碎屑橡胶干燥的经验模型和扩散模型,并研究诸如入口干燥温度,体积流量之类的干燥参数的影响。 ,以及初始含水量对干燥橡胶质量的影响。最后,利用入口空气流速为300-600 m〜3 / min-m〜3的碎胶(相当于1.8-5.0 m / s),建立了预测碎胶干燥动力学的数学干燥模型。橡胶厚度固定为0.25 m。样品的平均初始水分含量在40%至50%干基的范围内,而所需的最终水分含量在5%干基以下。结果表明,粒状胶的干燥方程与进气温度高度相关,而干燥常数与初始含水量不成正比。因此,使用九种经验模型来编制实验数据,并根据菲克扩散定律开发水分比方程的解析解。结果表明,仿真数据与对数模型最吻合,与实验数据基本吻合。粒状生胶的有效扩散系数在1.0 x 10〜(-9)至2.15 x 10〜(-5)m〜2 / s的范围内,分别对应于40至150°C的干燥温度。报告了空气再循环,入口干燥温度,初始水分含量,空气流速和干燥策略对比能耗和样品质量的影响。使用以下两种不同的干燥策略进行实验:一级和二级干燥条件。结果表明,初始含水量和空气流速显着影响橡胶的比能耗和质量,而体积空气流速对橡胶的比能耗起主导作用。模拟结果表明,与其他相比,再循环空气中90%至95%的百分比提供了最低的单位能耗。

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