Separation of propylene oxide-methanol-water mixture via enhanced extractive distillation: Design and control

Abstract The ternary azeotropic mixture of propylene oxide-methanol-water generally occurs in the direct oxidation of hydrogen peroxide and needs to be separated effectively. This paper explores two energy-efficient configurations with water as solvent, namely extractive dividing-wall column (EDWC) and side-stream extractive distillation (SSED), in terms of the potential economic advantages compared to conventional extractive distillation (CED) and the dynamic control. Several steady-state designs with the minimum total annual cost (TAC) by using a sequential iterative optimization method are achieved and compared. Regarding the controllability, four control structures for the SSED are developed and examined via introducing the feed flow and composition disturbances as well as one control structure for the EDWC. Similar to the EDWC, the SSED can be well controllable via an optimal control structure relying on only temperature measurements.

[1]  Changsheng Yang,et al.  Organic Salt Effect of Tetramethylammonium Bicarbonate on the Vapor–Liquid Equilibrium of the Methanol–Water System , 2011 .

[2]  W. Shen,et al.  Process Development, Assessment, and Control of Reactive Dividing-Wall Column with Vapor Recompression for Producing n-Propyl Acetate , 2018, Industrial & Engineering Chemistry Research.

[3]  Gabor Modla,et al.  Energy saving methods for the separation of a minimum boiling point azeotrope using an intermediate entrainer , 2013 .

[4]  Lanyi Sun,et al.  Energy-efficient separation process and control scheme for extractive distillation of ethanol-water using deep eutectic solvent , 2019, Separation and Purification Technology.

[5]  Ž. Olujić,et al.  Conceptual design of an internally heat integrated propylene-propane splitter , 2006 .

[6]  Hao Yu,et al.  Energy-saving dividing-wall column design and control for benzene extraction distillation via mixed entrainer , 2016 .

[7]  Yinglong Wang,et al.  Insight into pressure-swing distillation from azeotropic phenomenon to dynamic control , 2017 .

[8]  Xiaojing Shi,et al.  Comparison of heterogeneous azeotropic and pressure-swing distillations for separating the diisopropylether/isopropanol/water mixtures , 2019, Chemical Engineering Research and Design.

[9]  Lichun Dong,et al.  Design and control of pressure-swing distillation for separating ternary systems with three binary minimum azeotropes , 2019, AIChE Journal.

[10]  Jingzheng Ren,et al.  Investigation of energy-saving azeotropic dividing wall column to achieve cleaner production via heat exchanger network and heat pump technique , 2019, Journal of Cleaner Production.

[11]  Kang Ma,et al.  Energy-saving thermally coupled ternary extractive distillation process by combining with mixed entrainer for separating ternary mixture containing bioethanol , 2018 .

[12]  Yong Wang,et al.  Control of extractive distillation process for separating heterogenerous ternary azeotropic mixture via adjusting the solvent content , 2018 .

[13]  Aurangzeb,et al.  Pressure-Swing Dividing Wall Column with Multiple Binary Azeotropes: Improving Energy Efficiency and Cost Savings through Vapor Recompression , 2018 .

[14]  William L. Luyben,et al.  Control of a multiunit heterogeneous azeotropic distillation process , 2006 .

[15]  Mengxiao Yu,et al.  Control of an energy-saving side-stream extractive distillation process with different disturbance conditions , 2019, Separation and Purification Technology.

[16]  W. Luyben Control comparison of conventional extractive distillation with a new split-feed configuration , 2016 .

[17]  N. Zhang,et al.  Control of a Ternary Extractive Distillation Process with Recycle Splitting Using a Mixed Entrainer , 2018 .

[18]  Jiwei Qin,et al.  Design and Control of Extractive Dividing-Wall Column for Separating Ethyl Acetate–Isopropyl Alcohol Mixture , 2014 .

[19]  A. V. Morgunov,et al.  Application of the partially thermally coupled distillation flowsheets for the extractive distillation of ternary azeotropic mixtures , 2015 .

[20]  Lanyi Sun,et al.  Design and Control of Extractive Dividing Wall Column for Separating Benzene/Cyclohexane Mixtures , 2014 .

[21]  Elena Anokhina,et al.  Criterion of the energy effectiveness of extractive distillation in the partially thermally coupled columns , 2015 .

[22]  W. Shen,et al.  Improved design and optimization for separating tetrahydrofuran–water azeotrope through extractive distillation with and without heat integration by varying pressure , 2018 .

[23]  Xiaojing Shi,et al.  Comparison of pressure-swing distillation and heterogeneous azeotropic distillation for recovering benzene and isopropanol from wastewater , 2019, Process Safety and Environmental Protection.

[24]  Jun Gao,et al.  An improvement scheme for pressure-swing distillation with and without heat integration through an intermediate connection to achieve energy savings , 2018, Comput. Chem. Eng..

[25]  Chao Guang,et al.  Compared novel thermally coupled extractive distillation sequences for separating multi-azeotropic mixture of acetonitrile/benzene/methanol , 2018, Chemical Engineering Research and Design.

[26]  A. A. Kiss,et al.  Enhanced bioethanol dehydration by extractive and azeotropic distillation in dividing-wall columns , 2012 .

[27]  Chao Guang,et al.  Comparison of extractive distillation separation sequences for acetonitrile/methanol/benzene multi-azeotropic mixtures , 2018, Journal of Chemical Technology & Biotechnology.

[28]  Lichun Dong,et al.  Proportional-Integral Control and Model Predictive Control of Extractive Dividing-Wall Column Based on Temperature Differences , 2018, Industrial & Engineering Chemistry Research.

[29]  W. Shen,et al.  Comparative optimal design and control of two alternative approaches for separating heterogeneous mixtures isopropyl alcohol-isopropyl acetate-water with four azeotropes , 2019, Separation and Purification Technology.

[30]  Jun Gao,et al.  Application of Mixed Solvent To Achieve an Energy-Saving Hybrid Process Including Liquid–Liquid Extraction and Heterogeneous Azeotropic Distillation , 2019, Industrial & Engineering Chemistry Research.

[31]  W. Luyben Control comparison of conventional and thermally coupled ternary extractive distillation processes , 2016 .

[32]  K. Ma,et al.  Dynamic Control of Hybrid Processes with Liquid–Liquid Extraction for Propylene Glycol Methyl Ether Dehydration , 2018, Industrial & Engineering Chemistry Research.

[33]  Chao Guang,et al.  Economics and Controllability of Conventional and Intensified Extractive Distillation Configurations for Acetonitrile/Methanol/Benzene Mixtures , 2018, Industrial & Engineering Chemistry Research.

[34]  Anton A. Kiss,et al.  Innovative single step bioethanol dehydration in an extractive dividing-wall column , 2012 .

[35]  Arturo Jiménez-Gutiérrez,et al.  Design of an energy-efficient side-stream extractive distillation system , 2017, Comput. Chem. Eng..

[36]  Peizhe Cui,et al.  Design optimization and operating pressure effects in the separation of acetonitrile/methanol/water mixture by ternary extractive distillation , 2019, Journal of Cleaner Production.

[37]  Na Yu,et al.  Comparison of different extractive distillation processes for 2-methoxyethanol/toluene separation: Design and control , 2017, Comput. Chem. Eng..

[38]  Arturo Jiménez-Gutiérrez,et al.  Control analysis of an extractive dividing-wall column used for ethanol dehydration , 2014 .

[39]  Pravin D. Ghuge,et al.  Comparative analysis of extractive and pressure swing distillation for separation of THF-water separation , 2017, Comput. Chem. Eng..

[40]  Xiaohong Wang,et al.  Design and control of extractive dividing wall column and pressure-swing distillation for separating azeotropic mixture of acetonitrile/N-propanol , 2016 .

[41]  William L. Luyben,et al.  Evaluation of criteria for selecting temperature control trays in distillation columns , 2006 .

[42]  Jun Gao,et al.  Comparison of pressure-swing distillation with or without crossing curved-boundary for separating a multiazeotropic ternary mixture , 2019, Separation and Purification Technology.