PRESSURE-COMPENSATED TEMPERATURE CONTROL IN RECTIFICATION COLUMN

Norkobilov Adham, Zafar Safarovich Turakulov, Kamolov Azizbek, Talipov Hojiakbar
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Abstract

The focus of this work is to study the control of a rectification column (RC) for separating n-butane (nC4) and n-pentane (nC5) mixtures. Two control structures based on conventional temperature control (TC) and pressure-compensated control (PTC) structures are studied and compared using Aspentech software. The control performance of TC and PTC are investigated in terms of the control of component purities in both distillate and bottoms streams, under various disturbances in feed and pressure conditions. Due to pressure compensation, PTC is superior to TC in terms of purity and impurity control under disturbances in feed and pressure conditions. Accordingly, simulation results, from the point of view of industrial operation, the pressure-compensated temperature control (PTC) scheme provides potential solutions for a bicomponent RC.
精馏塔压力补偿温度控制
本工作的重点是研究分离正丁烷(nC4)和正戊烷(nC5)混合物的精馏塔的控制。利用Aspentech软件对基于常规温度控制(TC)和压力补偿控制(PTC)的两种控制结构进行了研究和比较。在进料和压力条件下的各种干扰下,从馏分流和底流中组分纯度的控制方面研究了TC和PTC的控制性能。由于压力补偿,在进料和压力条件下,PTC的纯度和杂质控制优于TC。因此,仿真结果表明,从工业运行的角度来看,压力补偿温度控制(PTC)方案为双组分RC提供了潜在的解决方案。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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