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Rectification tower with internal heat and mass exchange and method for separation of multi-component mixtures into fractions using a rectification tower with an internal heat and mass exchange

机译:具有内部热和质量交换的精馏塔以及使用具有内部热和质量交换的精馏塔将多组分混合物分离为馏分的方法

摘要

A rectification column for multi-component mixture separation with internal heat and mass exchange, which ensures a heat and mass exchange in the film mode with internal reflux generation along the whole length of heat and mass exchange tubes and which allows for an increased efficiency, is proposed. The rectification column includes the rectifying/enriching section with the heat and mass exchange in its tubular and annular spaces being topped by a heat carrier distributor with a distributor chamber (17) on top of the heat carrier distributor in such a way that a higher pressure of fluid heat carrier in the distributor chamber (17) than in the annular space is allowed. The design of the distributor allows to separate an upper outlet for heat carrier vapors and a lower outlet for liquid heat carrier from the annular space completely from the fluid supply of fluid heat carrier in the distributor chamber. A feed-in device allows the multi-component mixture to enter the tubular spaces from below. A device for liquid phase (from the multi-component mixture) discharge from the rectification column. A heating medium vessel may be connected to the annular space and steam condenser of the heat carrier medium. One or more additional lower rectification section/s (19) with the heat and mass exchange in its tubular space of the tubes being aligned with the tubes may be provided directly below the enriching section. A steaming section, wherein the tubes and may be equipped with turbulators. The rectification column permits to extract intermediate fractions of the separated mixture with the help of appropriate devices installed below the enriching section.
机译:一种用于内部热交换和质量交换的多组分混合物分离的精馏塔,它确保了膜模式下的热交换和质量交换,并在热交换和质量交换管的整个长度上产生内部回流,并提高了效率。建议。精馏塔包括一个精馏/富集部分,在其管状和环形空间中进行热量和质量交换,顶部是一个载热体分配器,在载热体分配器的顶部有一个分配室( 17 )。这样,允许分配器腔室( 17 )中的流体热载体的压力比环形空间中更高。分配器的设计允许将环形空间中用于载热蒸汽的上部出口和用于液态载热的下部出口与分配器腔中流体载热的流体供应完全分开。进料装置允许多组分混合物从下方进入管状空间。一种从精馏塔排出液相(来自多组分混合物)的装置。载热介质容器可以连接到载热介质的环形空间和蒸汽冷凝器。可在富集段的正下方设置一个或多个附加的下部精馏段( 19 ),在其管的管状空间中的热和质量交换与管对齐。蒸汽部分,其中所述管和可配备有湍流器。精馏塔允许借助于安装在富集区下方的适当装置来提取分离的混合物的中间馏分。

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