含水乙醇脱水

B. Tanaka, L. Otten
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引用次数: 7

摘要

将含水酒精升级为无水乙醇可以使用填充床吸附过程来完成,其中裂化谷物玉米是吸附剂。根据一系列台架实验获得的数据,设计并建造了直径0.35米乘3.0米的脱水塔。结果表明,谷物玉米可以以0.20L/min的速度将91%的乙醇转化为99%以上。原型中玉米床的容量范围为7.6至10.5 mL/kg,低于实验室规模实验的预期。这种差异归因于吸附热的显著热效应,从而导致床层温度升高。原型的性能是使用床的一维分散对流描述进行数学建模的。在热效应不明显的区域(其中C/C0<;0.5),观察到该模型很好地拟合了实验数据,并且在非等温区域显示出系统偏离。观察到脱水和再生循环的估计能耗低于通常与共沸蒸馏相关的能耗。除了能源优势外,吸附系统比共沸蒸馏更容易操作,也更安全。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Dehydration of aqueous ethanol

Upgrading of aqueous alcohol to anhydrous ethanol may be accomplished using a packed bed adsorption process, in which cracked grain corn is the adsorbent. A 0.35 m diameter by 3.0 m dehydration column was designed and constructed on the basis of data obtained in a series of bench-scale experiments.

The results demonstrated that grain corn would upgrade 91% ethanol to 99%-plus at a rate of about 0.20 L/min. The capacity of the corn bed in the prototype ranged from7.6 to 10.5 mL/kg of bed, which was lower than expected from the bench-scale experiments. The difference was attributed to the significant thermal effect of the heat of adsorption, which caused higher bed temperatures.

The performance of the prototype was modelled mathematically using a one-dimensional dispersive-convective description of the bed. The model was observed to fit the experimental data well in the regions where heat effects were not pronounced (where C/C0 < 0.5), and showed a systematic departure in the non-isothermal regions.

The estimated energy consumption for the dehydration and regeneration cycles was observed to be lower than that normally associated with azeotropic distillation. Aside from the energy advantage, an adsorption system is easier and safer to operate than azeotropic distillation.

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