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Liquid Drying by Solid Desiccant Materials: Experimental Study and Design Method

机译:固体干燥剂进行液体干燥的实验研究与设计方法

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The use of consumable solid desiccant materials for organic liquid dehydration is very current in refinery or chemistry processes, especially when the water concentration is very low ($<$1000?ppm). In spite of its common use, the kinetics of liquid drying by solid desiccants is not well known, and scale-up of industrial drying processes using such materials is always problematic. In this study, the kinetics of drying of two organic liquids, dipropylene-glycol (DPG) and toluene, with some classical “type-1” desiccant materials is analysed. The experiments were done on three different scales, by using different appropriate apparatus: a laboratory stirred reactor, a small pilot and a semi-industrial pilot. The results show that dehydration kinetics is driven by a strong mass transfer limitation. Based on these results, a simple model is developed in order to design industrial drying columns from pilot data. This model is able to predict the time evolution of the water content at the outlet of the column, and the resulting simulations are in good agreement with experiments.
机译:在炼油厂或化学过程中,特别是在水浓度非常低($ <$ 1000?ppm)的情况下,使用消耗性固体干燥剂材料进行有机液体脱水非常普遍。尽管通常使用固体干燥剂进行液体干燥的动力学尚不为人所知,并且使用这种材料进行工业干燥工艺的规模放大始终是有问题的。在这项研究中,分析了两种有机液体(丙二醇(DPG)和甲苯)与一些经典的“ 1型”干燥剂材料的干燥动力学。通过使用不同的适当设备,在三种不同规模下进行了实验:实验室搅拌反应器,小型中试和半工业中试。结果表明,脱水动力学受强大的传质限制的驱动。基于这些结果,开发了一个简单的模型,以便根据试验数据设计工业干燥塔。该模型能够预测色谱柱出口处水含量的时间演变,并且所得的模拟结果与实验非常吻合。

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