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Determination of the drying rate and effective diffusivity coefficients during convective drying of two-phase olive mill waste at rotary dryers drying conditions for their application

机译:在旋转干燥器干燥条件下对两相橄榄磨废干燥期间干燥率和有效扩散系数的干燥率和有效扩散系数

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Secondary extraction factories in the oil olive production are subjected to high pressures each year due to the treatment of large quantities of olive mill wastes. In return, this sector achieves a biomass by-product and olive pomace oil. Furthermore, these facilities remove a serious environmental problem. To help improve and optimize the drying process of these wastes, we have carried out a study of mass transfer in a convective dryer using the drying conditions in rotary dryers. A design of experiments based on a central composite design in two dimensions, drying air temperature (between 100 degrees C and 425 degrees C) and drying air velocity (between 1 m/s and 7 m/s), was used to determine the drying rate and effective diffusivity coefficients. These variables were calculated from the experimental data obtained in isothermal drying test. Polynomial surface models, obtained by the linear least-squares fitting method, allowed to calculate these variables as a function of other such as drying air temperature, drying air velocity and moisture ratio. Drying rate and effective diffusivity values were found between 0.00001915 and 0.028 kg(water)/kg(solid).s and 1.917.10(-8) and 10.02.10(-8) m(2)/s, respectively. These parameters will contribute to solve the heat and mass transfer phenomena in rotary dryers. (C) 2020 Elsevier Ltd. All rights reserved.
机译:由于大量橄榄磨废物的处理,每年的石油橄榄产量中的二次提取工厂每年都受到高压。作为回报,该部门达到了生物量副产物和橄榄渣油。此外,这些设施消除了严重的环境问题。为了帮助改善和优化这些废物的干燥过程,我们使用旋转式干燥器中的干燥条件进行了对流干燥器中的传质转移的研究。基于两个尺寸的中央复合设计的实验设计,干燥空气温度(100℃和425℃)和干燥空气速度(在1米/秒和7米之间)来确定干燥速率和有效的扩散系数。这些变量由在等温干燥试验中获得的实验数据计算。多项式表面模型由线性最小二乘拟合方法获得,允许作为其他变化的诸如干燥空气温度,干燥空气速度和水分比的函数来计算这些变量。在0.00001915和0.028kg(水)/ kg(固体)之间发现干燥速率和有效扩散值分别为1.917.10(-8)和10.02.10(-8)m(2)/ s。这些参数将有助于解决旋转式干燥器中的热量和传质现象。 (c)2020 elestvier有限公司保留所有权利。

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