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Drying sago pith waste in a fluidized bed dryer

机译:在流化床烘干机中干燥Sago Pith废物

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Sago pith waste produced in largely during the manufacturing process of sago flour and causes serious environmental pollution. Once SPW is dried, it can be stored and further exploited for its high starch content. SPW has an original moisture content of 90% wet basis but can be dried to 10% wet basis. This study evaluated the effects of the bulk and tapped densities on the moisture content of SPW and used the compressibility index and Hausner ratio to characterize the flow of SPW in a fluidized bed dryer at wet basis. The temperature (50-80 degrees C) and velocity (1.5-2.1 m/s) of the air supplied into the fluidized bed dryer were considered in terms of the loss of moisture content, drying rate, and fluidization profile of the drying process. The effective moisture diffusivity were estimated to determine the optimum drying condition. The experimental results showed that the drying process took less time and reached a higher drying rate as the air temperature and velocity increased. Increasing the air temperature increased the heat transfer between SPW and dry air and accelerated the movement of moisture to the surface. The air velocity had a less significant effect on the drying process and was more important for fluidization of the SPW. The profile showed a fixed bed during early fluidization, followed by a bubbling state and then turbulent condition. Increasing the air temperature reduced the time for SPW to reach turbulent situation. Increasing the air velocity increased the bubbling fluidization density and accelerated the turbulent fluidization. Based on the effective moisture diffusivity analysis, it showed that the optimum drying process of SPW could be achieved at air velocity of 1.50 m/s with 80 degrees C of air temperature and at air temperature of 70 degrees C with 2.10 m/s of air velocity. Meanwhile, dry sieve analysis was performed to obtain the particle size distribution and percentage of fines in SPW with the sieve sizes of 3.35, 2.00, 1.70, 1.00, 0.85, 0.60, and 0.43 mm. Then, SPW was classified and characterized according to each particle size range. Visually, SPW was found to have three categories of particles: sand, gravel, and fibrous wood. (C) 2020 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:Sago Pith废物主要在Sago粉的制造过程中产生,并导致严重的环境污染。一旦SPW干燥,它可以被储存并进一步利用其高淀粉含量。 SPW的原始水分含量为90%湿基础,但可以干燥至10%湿法。该研究评估了体积和截止密度对SPW的水分含量的影响,并使用压缩指数和Hausner比率在湿法的过程中表征流化床干燥器中的SPW流。在流化床干燥器中的损失,干燥过程的流化曲线损失方面考虑了在流化床干燥器中提供的空气的温度(50-80℃)和速度(1.5-2.1m / s)。估计有效的水分扩散率以确定最佳干燥条件。实验结果表明,随着空气温度和速度增加,干燥过程花费较少的时间并达到更高的干燥速率。增加空气温度增加了SPW和干燥空气之间的热传递,并加速了水分的运动到表面。空气速度对干燥过程具有较小的效果,对SPW的流化更重要。该轮廓在早期流化期间展示了固定床,然后是鼓泡状态,然后是湍流状态。增加空气温度降低了SPW达到湍流情况的时间。增加空气速度提高了起泡的流化密度并加速了湍流流化。基于有效的水分扩散性分析,表明,SPW的最佳干燥过程可以在1.50米/秒的空气速度下实现,空气温度为80℃,空气温度为70℃,空气2.10米/米速度。同时,进行干筛分分析以获得SPW中的粒度分布和筛分粒度,筛例尺寸为3.35,2.00,1.70,1.00,0.85,0.60和0.43mm。然后,根据每个粒度范围进行分类和表征SPW。目视,SPW被发现有三类粒子:沙,砾石和纤维木。 (c)2020化学工程师机构。 elsevier b.v出版。保留所有权利。

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