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Nonlinear Wave Modeling and DynamicAnalysis of Internal Thermally CoupledDistillation Columns

机译:内部热耦合蒸馏塔的非线性波动建模和动力学分析

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Internal thermally coupled distillation column (LTCDIC) is a frontier in the energy saving distillation research. It is well known for the complex dynamics, which challenge the establishment of an excellent reduced model for further control strategy design greatly. In this article, a physical approach of the LTCDIC process based on nonlinear wave theory is explored, where it is first discovered that traditional wave theory in conventional distillation columns (CDIC) could not be directly applied in LTCDIC, due to: First, the internal thermal coupling results in mole flow rates varying evidently over each stage, which not only makes the wave modeling of the wave phenomenon in LTCDIC more difficult but also makes wave dynamics greatly different between LTCDIC and CDIC; Second, an interesting wave phenomenon of LTCDIC is discovered that waves located in the rectifying section and stripping section travel under opposite tendencies when the steady state is disturbed by the step change of thermal condition q, one sharpens and the other is likely to spread synchronously, it means the movement of wave profiles in LTCDIC could not be simply described by shock wave velocity, which is usually used in wave modeling of CDIC; more seriously, shapes of the self-sharpening wave profiles in ITCDIC change obviously during the traveling processes, which further reveals that shape influence on wave velocity has to be considered in the wave modeling of LTCDIC. A rigorous wave velocity and a natural wave velocity are derived, respectively, based on which, the detailed analyses of traveling wave characteristics are carried out. A novel wave velocity, based on the profile trial function which has been well developed by Marquardt, is further derived to consider the obvious change of profile shape. And a completed nonlinear wave model of ITCDIC is thereby established by combining the proposed wave velocity with thermal coupling relations and material balance relations. The benzene-toluene system is illustrated as an example, where component concentration prediction and distinct dynamic characteristics are carried out in detail based on the proposed nonlinear wave models. The research results reveal the accuracy and validity of the proposed nonlinear wave model of LTCDIC.
机译:内部热耦合蒸馏塔(LTCDIC)是节能蒸馏研究的前沿领域。众所周知,复杂的动力学对建立一个精简的简化模型以进一步控制策略设计提出了挑战。本文探讨了基于非线性波动理论的LTCDIC过程的物理方法,首先发现传统蒸馏塔(CDIC)中的传统波动理论不能直接应用于LTCDIC,原因如下:首先,内部热耦合导致摩尔流速在每个阶段明显变化,这不仅使LTCDIC中的波浪现象的波浪建模更加困难,而且使LTCDIC和CDIC之间的波浪动力学差异很大。其次,发现了LTCDIC的一种有趣的波动现象,当稳态受热条件q的阶跃变化干扰时,位于精馏段和汽提段的波以相反的趋势行进,一个变尖,另一个很可能同步传播,这意味着LTCDIC中的波剖面运动不能简单地用冲击波速度来描述,这通常用于CDIC的波模型中。更严重的是,ITCDIC中自锐波剖面的形状在行进过程中会发生明显变化,这进一步表明,在LTCDIC的波浪建模中必须考虑形状对波速的影响。分别推导了严格的波速和自然波速,在此基础上,进行了行波特性的详细分析。考虑到轮廓形状的明显变化,进一步推导了一种新的波速,该波速基于Marquardt精心开发的轮廓试验函数。通过将拟议的波速与热耦合关系和材料平衡关系相结合,建立了完整的ITCDIC非线性波动模型。以苯-甲苯系统为例,其中基于所提出的非线性波模型详细进行了组分浓度预测和明显的动态特性。研究结果揭示了所提出的LTCDIC非线性波动模型的准确性和有效性。

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