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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Control of reflux and reboil flow rates for milli and micro distillation
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Control of reflux and reboil flow rates for milli and micro distillation

机译:控制毫蒸馏和微蒸馏的回流和再沸流速

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摘要

An accurate control of reflux and reboil flow rates for small scale distillation unit has been evaluated. Its feasibility was studied with a distillation column with good results. The distillation column was planar in shape, and it was operated in a horizontal orientation. Porous, open-cell metal foam was used as the column packing. The distillation unit could be operated at extremely low mass fluxes. The operation of the distillation unit was extremely stable, which was achieved thanks to the rigorous control of the fluid flow rates, and heat losses. The heat loss model was regressed based on distillation experiments with total reflux, and the model was used to optimize the temperature of the column shell in order to minimize the heat losses from the column. The volume of the reboiler, the preheaters, and the heat exchangers was minimized with the use of flat channels for intensified heat exchange. The total liquid holdup of the system was less than 40 cm~3. The efficiency of the distillation unit was characterized for two binary and one ternary system.
机译:评估了小型蒸馏装置的回流和再沸流量的精确控制。用蒸馏塔研究了其可行性,并取得了良好的效果。蒸馏塔为平面形状,并且在水平方向上操作。多孔的开孔金属泡沫被用作柱填料。蒸馏单元可以在极低的质量流量下运行。蒸馏单元的运行极为稳定,这要归功于对流体流速和热量损失的严格控制。根据具有全回流的蒸馏实验对热损失模型进行回归,并使用该模型优化塔壳温度,以最大程度地减少塔的热损失。再沸器,预热器和热交换器的体积通过使用扁平通道进行加强的热交换而得以最小化。系统的总持液量小于40 cm〜3。对于两个二元体系和一个三元体系,对蒸馏单元的效率进行了表征。

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