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Insight into pressure-swing distillation from azeotropic phenomenon to dynamic control

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TLDR
In this article, the authors describe the development of pressure-swing distillation (PSD), including all of the main aspects related to thermodynamic analysis, Quantitative structure property relationship (QSPR), process design, process intensification, and dynamic control.
Abstract
Pressure-swing distillation (PSD) is widely used as an efficient method for separating pressure-sensitive azeotropic mixtures in industrial processes. Remarkably, PSD can achieve pure products without introducing a third component compared with extractive distillation and azeotropic distillation. Heat integration into PSD can save energy and reduce operating costs, thus relieving the continuous growth of energy consumption in the distillation industry. This review paper describes the development of this widely used distillation technique, including all of the main aspects related to thermodynamic analysis, Quantitative structure property relationship (QSPR), process design, process intensification, and dynamic control. Based on the foundation of research, further development of PSD is proposed for separating multi-component azeotropic mixtures and exploring the process design and dynamic control from QSPR, aiming at promoting the industrial application of this environmentally friendly and well-known separation technique from multi-scale analysis.

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Citations
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Journal ArticleDOI

An overview of process systems engineering approaches for process intensification: State of the art

TL;DR: An overview of the development of various process intensification technologies, specifically those under the categories of separation, reaction, hybrid reaction/separation, and alternative energy sources are provided.
Journal ArticleDOI

Energy-saving thermally coupled ternary extractive distillation process by combining with mixed entrainer for separating ternary mixture containing bioethanol

TL;DR: In this paper, two thermally coupled ternary extractive distillation processes were studied to separate the Ternary azeotropic mixture tetrahydrofuran/ethanol/water using a single component solvent (dimethyl sulfoxide) and a mixed solvent(dimethyl sulphoxide and ethylene glycol) as entrainer.
Journal ArticleDOI

Review of Extractive Distillation. Process design, operation optimization and control

TL;DR: In this article, the authors define extractive separation classes that summarize feasibility regions, achievable products and entrainer-feed flow rate ratio limits for different types of entrainers.
Journal ArticleDOI

Optimal Design and Effective Control of Triple-Column Extractive Distillation for Separating Ethyl Acetate/Ethanol/Water with Multiazeotrope

TL;DR: The separation of the ternary nonideal system with multiazeotropes is discussed in this article, where the authors show that they are always generated in the production process of n-butanol.
Journal ArticleDOI

Design optimization and operating pressure effects in the separation of acetonitrile/methanol/water mixture by ternary extractive distillation

TL;DR: In this article, a novel sequential iterative optimization methodology is proposed and the isovolatility curves of systems at different pressures are analyzed to investigate the effect of the operating pressure on the ternary extractive distillation process.
References
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Book

Perry's Chemical Engineers' Handbook

TL;DR: In this paper, conversion factors and mathematical symbols are used to describe conversion factors in physical and chemical data and Mathematical Symbols are used for converting, converting, and utilising conversion factors.

Perrys chemical engineers handbook

TL;DR: Perry's Chemical Engineers' Handbook as mentioned in this paper is a free download pdf for chemical engineering applications, from the fundamentals to details on computer applications and control, and it can be found in any computer science course.
Journal ArticleDOI

Local compositions in thermodynamic excess functions for liquid mixtures

TL;DR: In this paper, a new equation based on Scott's two-liquid model and on an assumption of nonrandomness similar to that used by Wilson is derived, which gives an excellent representation of many types of liquid mixtures.
Journal ArticleDOI

Optimum Settings for Automatic Controllers

TL;DR: In this paper, the three principal control effects found in present controllers are examined and practical names and units of measurement are proposed for each effect and corresponding units for a classification of industrial processes in terms of two principal characteristics affecting their controllability.
Journal ArticleDOI

Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systems

TL;DR: The UNIQUAC equation as discussed by the authors is a semi-theoretical equation for the excess Gibbs energy of a liquid mixture, which is generalized through introduction of the local area fraction as the primary concentration variable.
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