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Journal articles on the topic 'BINARY DISTILLATION COLUMN'

Author: Grafiati

Published: 11 September 2023

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1

P, Akhila. "Mathematical Modelling of Binary Distillation Column for Petrochemical Industries." International Journal for Research in Applied Science and Engineering Technology 10, no. 8 (2022): 926–31. http://dx.doi.org/10.22214/ijraset.2022.46309.

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Abstract: Distillation is a method of separating mixtures based on differences in volatility of components in a boiling liquid mixture. It is defined as a process in which a liquid or vapour mixture of two or more substance is separated in to component fractions of desired purity by the application and removal of heat. In this work importance is given to Binary distillation columns. In the Binary Distillation, the feed to the process consist of mixture of two components (A & B) and after the distillation two products will be generated. It is very important to model a distillation column an

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2

Raeva, V. M., and D. I. Sukhov. "SELECTION OF EXTRACTIVE AGENTS FOR THE SEPARATION OF CHLOROFORM - METHANOL - TETRAHYDROFURAN MIXTURE." Fine Chemical Technologies 13, no. 3 (2018): 30–40. http://dx.doi.org/10.32362/24106593-2018-13-3-30-40.

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Variants of the extractive distillation of chloroform - methanol - tetrahydrofuran equimolar mixture with industrial separating agents are considered. The basic system shows opposite deviations from the ideal behavior, because it contains binary azeotropes with minimum and maximum boiling points (3.3.1-4 system according to Serafimov’s classification). The choice of selective substances for extractive distillation was carried out taking into account the concentration dependences of the excess molar Gibbs energy of the binary constituents of the derivative system “chloroform - methanol - tetrah

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3

URIBE, LEOPOLDO BÁRCENAS, and JOAQUÍN ALVAREZ GALLEGOS. "Identification of a binary distillation column." International Journal of Systems Science 17, no. 2 (1986): 295–304. http://dx.doi.org/10.1080/00207728608926804.

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4

Alekseev, К. А., S. M. Kirichenko, А. V. Rakov, et al. "An Approach to Stabilize the Composition of Heavy Vacuum Gas Oil in the Production of Lubricating Oils." Chemistry and Technology of Fuels and Oils 630, no. 2 (2022): 8–13. http://dx.doi.org/10.32935/0023-1169-2022-630-2-8-13.

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A heavy vacuum gas oil separation unit was developed and implemented at an industrial enterprise with a stabilized composition. The technical solutions, the selected equipment and the results of the installation operation are described. On a laboratory model of a distillation column, experiments were made to develop technological conditions. In calculations of an industrial column with a new regular packing applied previously developed mathematical model of multicomponent distillaton. The mixture is represented as pseudo-binary in terms of fractions. In addition, software packages for plate-by

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5

Zbytovský, Jiří, Tomáš Sommer, Martin Zapletal, and Jiří Trejbal. "Comparison of various column packing materials efficiency for hydrocarbons and aqueous mixtures." Chemical & biochemical engineering quarterly 33, no. 2 (2019): 183–90. http://dx.doi.org/10.15255/cabeq.2018.1565.

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The efficiency of industrial column packings is commonly tested by standard hydrocarbon mixtures. However, a reduced efficiency value is often observed, particularly during distillation of aqueous mixtures. In this paper, distillation experiments with various binary mixtures were carried out on different column packings to evaluate relative separation efficiencies of mixtures for each packing material. Each of the binary mixtures, which comprised heptane–methylcyclohexane, ethanol–water, morpholine–water, and acetic acid–water, was distilled under atmospheric pressure and total reflux ratio on

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6

Zakharov, Mikhail K., Yuri A. Pisarenko, and Oksana I. Sycheva. "COMPARISON OF ENERGY SAVING METHODS FOR DISTILLATION OF LIQUID MIXTURES." IZVESTIYA VYSSHIKH UCHEBNYKH ZAVEDENII KHIMIYA KHIMICHESKAYA TEKHNOLOGIYA 64, no. 1 (2020): 85–92. http://dx.doi.org/10.6060/ivkkt.20216401.6141.

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The analysis and review of the scientific literature on methods and approaches to energy saving in distillation, as one of the most energy-intensive processes for the separation of binary and multicomponent mixtures was carried out. Directions of the scientific literature are highlighted, showing the relevance of the thermodynamic method assessment of separation processes. A comparative analysis of various methods of energy conservation in the separation of liquid binary mixtures by the distillation method is performed (a binary mixture of benzene-toluene was chosen as an example). A conventio

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7

Zakharov, Mikhail K., Yuri A. Pisarenko, and Oksana I. Sycheva. "COMPARISON OF ENERGY SAVING METHODS FOR DISTILLATION OF LIQUID MIXTURES." IZVESTIYA VYSSHIKH UCHEBNYKH ZAVEDENII KHIMIYA KHIMICHESKAYA TEKHNOLOGIYA 64, no. 1 (2020): 85–92. http://dx.doi.org/10.6060/ivkkt.20216401.6141.

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The analysis and review of the scientific literature on methods and approaches to energy saving in distillation, as one of the most energy-intensive processes for the separation of binary and multicomponent mixtures was carried out. Directions of the scientific literature are highlighted, showing the relevance of the thermodynamic method assessment of separation processes. A comparative analysis of various methods of energy conservation in the separation of liquid binary mixtures by the distillation method is performed (a binary mixture of benzene-toluene was chosen as an example). A conventio

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8

CHEKARI, Tassadit, Rachid MANSOURI, and Maamar BETTAYEB. "IMC-PID-FOF Multi-loop controller design for Binary Distillation Column." Algerian Journal of Signals and Systems 7, no. 1 (2022): 13–20. http://dx.doi.org/10.51485/ajss.v7i1.155.

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This paper deals with the fractional order multi-loop controller design for a distillation column. The idea is a generalization of the IMC-PID-FOF controller design method developed for monovariable systems to the distillation column model which is multivariable. The principle is based on the IMC paradigm and the choice of appropriate control configuration with minimum of interactions. The proposed method is illustrated with an example of a distillation column model taken from the literature.

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9

Papastathopoulou, Heleni S., and William L. Luyben. "Control of a binary sidestream distillation column." Industrial & Engineering Chemistry Research 30, no. 4 (1991): 705–13. http://dx.doi.org/10.1021/ie00052a013.

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10

Peréz-Gallegos, Iván, Victor M. Rivera, Eliseo Hernandez-Martinez, and Claudio B. Arroyo. "Integration of design and control for distillation columns through dynamic optimization." Memorias del Congreso Nacional de Control Automático 5, no. 1 (2022): 469–73. http://dx.doi.org/10.58571/cnca.amca.2022.088.

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In this work, a methodology for the integration of design and control methods for distillation columns through dynamic optimization tools is proposed. For this, a dynamic model of the distillation column that can be adapted to different mixtures (binary and multicomponent) is established. The proposal focuses on defining an objective function to simultaneously maximize the performance in the mixture separation under the lowest energy consumption. The design variables (i.e., number of trays and feeding stage), as well as the controller parameters, are considered as decision variables. The resul

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11

Zakharov, M. K., A. V. Egorov, and A. A. Podmetenny. "Liquid mixtures separation and heat consumption in the process of distillation." Fine Chemical Technologies 16, no. 1 (2021): 7–15. http://dx.doi.org/10.32362/2410-6593-2021-16-1-7-15.

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Objectives. The aim of this study is to investigate different distillation modes of a binary ideal mixture and determine how various factors affect heat consumption in the column boilers. In addition, it intends to assess the difficulty of separating mixtures. Our research is based on analyzing the characteristics of vapor-liquid equilibrium.Methods. To conduct our study, we used a graphic-analytical tool to calculate the distillation process of a binary mixture and mathematical models based on the Aspen Plus software package along with DSTWU, RadFrac, and the Sensitivity module. We also used

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12

BENDIB, Riad, Noual BATOUT, and Abdelmajid KHELASSI. "Design of Effective Control Schemes for Binary Distillation Columns." Algerian Journal of Signals and Systems 2, no. 4 (2017): 248–54. http://dx.doi.org/10.51485/ajss.v2i4.50.

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Distillation column is very important and high consuming energy equipment in oil refineries, such that 3% of the energy consumption in the world is allocated in distillation column. The fact that let controlling the distillation column an attractive field for researcher, and hence different control schemes are proposed by researchers. In this paper we will provide a comparative study between different control schemes for a binary distillation column two simple configurations (the most known ones) (LV&DV) and two more complicated ones ((L/D,V/B) & Ryskamp’s) we compare them in the basis

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13

Mendez-B, Juancarlos, Gilberto Gonzalez-Avalos, Noe Barrera Gallegos, Gerardo Ayala-Jaimes, and Carlos Rubio-Maya. "Modeling and Simulation of an Energy Integrated Distillation Column in a Bond Graph Approach." Entropy 24, no. 9 (2022): 1191. http://dx.doi.org/10.3390/e24091191.

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The bond graph methodology for modelling an integrated energy distillation column is applied in this paper. The distillation column is built by five trays for a binary mixture. However, due to its modular construction in a bond graph, the number of trays can be increased. In order to link the analysis tools of systems modeled in the bond graph to the mathematical model given to a distillation column, a junction structure of the proposed bond graph is presented. Hence, this junction structure is a way to obtain the state space representation of the modeled column in bond graphs. Likewise, it is

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14

Zhao, Shuo, Peng Bai, Xianghai Guo, Ke Tang, and Guangzhong Li. "Time requirements in closed and open batch distillation arrangements for separation of a binary mixture." Polish Journal of Chemical Technology 16, no. 4 (2014): 66–74. http://dx.doi.org/10.2478/pjct-2014-0072.

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Abstract Batch time requirements are provided for the separation of binary zeotropic mixtures in two different multivessel columns (with and without vapor bypass), a non-cyclic two-vessel column and a regular batch column based on dynamic simulations. The first three columns are operated as closed (total reflux) systems and the regular batch column is operated as an open (partial reflux) system. We analyze the effects of feed composition, relative volatility and product specification on the time requirements. The multivessel arrangements perform better than the regular batch column, which requ

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15

Ahmed Alawad, Nasir, and Afaf Jebar Muter. "Optimal Control of Model Reduction Binary Distillation Column." International Journal of Modern Education and Computer Science 13, no. 1 (2021): 59–68. http://dx.doi.org/10.5815/ijmecs.2021.01.05.

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16

Anozie, A. N., F. N. Osuolale, and A. S. Osunleke. "Exergy analysis of binary plate distillation column operations." International Journal of Exergy 6, no. 5 (2009): 715. http://dx.doi.org/10.1504/ijex.2009.027498.

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17

Kim, Young Han, and Jung Soo Kim. "Constrained Nonlinear Control of a Binary Distillation Column." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 31, no. 3 (1998): 417–24. http://dx.doi.org/10.1252/jcej.31.417.

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18

Castellanos-Sahagún, Eduardo, and Jesús Alvarez. "Binary Distillation Column Startup Using Two Temperature Measurements." Industrial & Engineering Chemistry Research 50, no. 10 (2011): 6187–204. http://dx.doi.org/10.1021/ie101659w.

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19

Soliman, Moustafa A. "A Shortcut Method for Binary Distillation Column Design." Journal of King Saud University - Engineering Sciences 21, no. 1 (2009): 1–4. http://dx.doi.org/10.1016/s1018-3639(18)30517-8.

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20

Sanchez, G., J. M. Dion, and L. Dugard. "Multivariable Adaptive Control of a Binary Distillation Column." IFAC Proceedings Volumes 18, no. 15 (1985): 171–76. http://dx.doi.org/10.1016/b978-0-08-033431-8.50033-6.

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21

Andersen, Henrik Weisberg, Mogens Kümmel, and Sten Bay Jørgensen. "Dynamics and identification of a binary distillation column." Chemical Engineering Science 44, no. 11 (1989): 2571–81. http://dx.doi.org/10.1016/0009-2509(89)85201-7.

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22

Andersen, Henrik Weisberg, and Kümmel Mogens. "Discrete-time control of a binary distillation column." Chemical Engineering Science 44, no. 11 (1989): 2583–95. http://dx.doi.org/10.1016/0009-2509(89)85202-9.

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23

Luus, Rein. "Time Optimal Control of a Binary Distillation Column." Developments in Chemical Engineering and Mineral Processing 10, no. 1-2 (2008): 19–31. http://dx.doi.org/10.1002/apj.5500100103.

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24

Ramezani, Mohammad Hossein, and Nasser Sadati. "Hierarchical optimal control of a binary distillation column." Optimal Control Applications and Methods 40, no. 1 (2018): 172–85. http://dx.doi.org/10.1002/oca.2473.

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25

Raeva, V. M., and A. M. Dubrovsky. "Comparison of extractive distillation flowsheets for methanol–tetrahydrofuran–water mixtures." Fine Chemical Technologies 15, no. 3 (2020): 21–30. http://dx.doi.org/10.32362/2410-6593-2020-15-3-21-30.

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Objectives. Synthesis and comparative analysis of the extractive distillation flowsheets for aqueous mixtures of solvents utilized in pharmaceutical industries using the example of a methanol−tetrahydrofuran−water system with various compositions. The ternary system contains two minimally boiling azeotropes that exist in a vapor–liquid phase equilibrium. To evaluate the selective effect of glycerol, the phase equilibria of the methanol–tetrahydrofuran–water and methanol–tetrahydrofuran–water–glycerol systems at 101.32 kPa were studied.Methods. The calculations were carried out in the Aspen Plu

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26

Sutijan, Sutijan, Megan Jobson, and Robin Smith. "Synthesis of Ternary Homogeneous Azeotropic Distillation Sequences: 2. Flowsheet Identification." ASEAN Journal of Chemical Engineering 13, no. 1 (2013): 43. http://dx.doi.org/10.22146/ajche.49724.

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This paper presents a systematic methodology for flowsheet generation for separating binary azeotropic mixtures using homogeneous azeotropic distillation. A new classification system for ternary mixtures using ‘standard distillation line maps’ defined in Sutijan et al. (2012) is employed. The new characterisation system is able to link candidate entrainers to flowsheet structures which can facilitate the separation. The sequences considered include pressure-swing distillation, two and three-column flowsheets with or without boundary crossing and the use of single and double-feed columns. For a

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27

Singh, Amit Kumar, Barjeev Tyagi, and Vishal Kumar. "First Principle Modeling and Neural Network–Based Empirical Modeling with Experimental Validation of Binary Distillation Column." Chemical Product and Process Modeling 8, no. 1 (2013): 53–70. http://dx.doi.org/10.1515/cppm-2013-0011.

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Abstract To get the better product quality and to decrease the energy consumption of the distillation column, an accurate and suitable nonlinear model is crucial important. In this work, two types of model have been developed for an existing experimental setup of continuous binary distillation column (BDC). First model is a theoretical tray-to-tray binary distillation model for describing the steady-state behavior of composition in response to changes in reflux flows and in reboiler duty. Another model is an artificial neural network (ANN)–based input/output data relationship model. In ANN-bas

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28

RIX, ARMIN, KATHARINA LÖWE, and HORST GELBE. "FEEDFORWARD CONTROL OF A BINARY HIGH PURITY DISTILLATION COLUMN." Chemical Engineering Communications 159, no. 1 (1997): 105–18. http://dx.doi.org/10.1080/00986449708936596.

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29

Kim, Young Han, Moo Hong Kim, and Ju Bong Kim. "Minimum Deviation Adaptive Control of a Binary Distillation Column." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 27, no. 2 (1994): 253–56. http://dx.doi.org/10.1252/jcej.27.253.

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30

Kim, Young Han, and Sun Ho Song. "Constrained Generalized Predictive Control of a Binary Distillation Column." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 29, no. 5 (1996): 760–66. http://dx.doi.org/10.1252/jcej.29.760.

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31

Vagi, F., R. K. Wood, A. J. Morris, and M. Tham. "Multivariable Self-tuning Control of a Binary Distillation Column." IFAC Proceedings Volumes 18, no. 11 (1985): 207–15. http://dx.doi.org/10.1016/s1474-6670(17)60129-0.

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32

Pullinen, R., and J. Lieslehto. "Multivariable Pi-Controller Tuning for a Binary Distillation Column." IFAC Proceedings Volumes 26, no. 2 (1993): 1–4. http://dx.doi.org/10.1016/s1474-6670(17)48415-1.

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33

Musch, H. E., та M. Steiner. "μ-Optimal Control of an Industrial Binary Distillation Column". IFAC Proceedings Volumes 26, № 2 (1993): 5–10. http://dx.doi.org/10.1016/s1474-6670(17)48416-3.

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34

Baratti, Roberto, Massimiliano Barolo, Fabrizio Bezzo, and Stefania Tronci. "Robust Dynamic State Estimation of a Binary Distillation Column." IFAC Proceedings Volumes 37, no. 9 (2004): 971–76. http://dx.doi.org/10.1016/s1474-6670(17)31934-1.

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35

Castro, Rafael, Jaime Alvarez, and Joaquin Alvarez. "Nonlinear disturbance decoupling control of a binary distillation column." Automatica 26, no. 3 (1990): 567–72. http://dx.doi.org/10.1016/0005-1098(90)90027-f.

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36

TOLEDO, BERNARDINO CASTILLO, and JOAQUÍN ALVAREZ GALLEGOS. "Identification and bilinear control of a binary distillation column." International Journal of Systems Science 18, no. 12 (1987): 2209–28. http://dx.doi.org/10.1080/00207728708967182.

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37

Trotta, A. "Nonlinear model-based control of a binary distillation column." Computers & Chemical Engineering 19, no. 1 (1995): S519—S524. http://dx.doi.org/10.1016/0098-1354(95)00068-d.

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38

Trotta, Antonio, and Massimiliano Barolo. "Nonlinear model-based control of a binary distillation column." Computers & Chemical Engineering 19 (June 1995): 519–24. http://dx.doi.org/10.1016/0098-1354(95)87089-x.

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39

Cingara, Aleksandar, Miodrag Jovanovic, and Milan Mitrovic. "Analytical first-order dynamic model of binary distillation column." Chemical Engineering Science 45, no. 12 (1990): 3585–92. http://dx.doi.org/10.1016/0009-2509(90)87161-k.

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40

Sharma, Ayush, Ján Drgoňa, Deepak Ingole, et al. "Teaching Classical and Advanced Control of Binary Distillation Column." IFAC-PapersOnLine 49, no. 6 (2016): 348–53. http://dx.doi.org/10.1016/j.ifacol.2016.07.202.

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41

Serafimov, L. A., and K. A. Morozov. "DISTILLATION OF BINARY TWO-PHASE MIXTURES WITH VARIOUS PHYSICO-CHEMICAL PROPERTIES: NORMAL MODE AND DEVIATIONS FROM IT." Fine Chemical Technologies 11, no. 4 (2016): 15–25. http://dx.doi.org/10.32362/2410-6593-2016-11-4-15-25.

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In this article, the normal continuous mode of distillation is considered using an example of binary two-phase mixture distillation. In practice, there are often deviations from the normal mode. It has been proved that the deviation leads to an increase in energy consumption for the ongoing process. In the industry, columns separating binary mixtures are normally the finishing apparatuses in the flow-sheet separation of multicomponent mixtures, which are obtained in the reactor as a result of main reactions as well as by-reactions. The distillation of binary mixtures is relatively simpler than

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42

Henrique, João Paulo, Ruy de Sousa Jr., Argimiro Resende Secchi, Mauro Antonio da Silva Sá Ravagnani, Abdessamad Barbara, and Caliane Bastos Borba Costa. "Divided Wall Column Modeling and Simulation in an Open-Source Environment." Chemical & biochemical engineering quarterly 34, no. 3 (2020): 149–67. http://dx.doi.org/10.15255/cabeq.2020.1824.

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The divided wall column (DWC) can achieve sharp separations of three or more components in a single shell, substituting conventional sequences of two or more binary<br /> distillation columns, with lower expenses. Despite these advantages, DWC models are not available in commercial chemical process simulators. To simulate DWC, users must employ instances of conventional column model and couple them in different configurations. In this paper, a DWC model was developed in EMSO (Environment for Modeling, Simulation and Optimization). DWC model was then used for simulating the separation of

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43

Hu, Zehua, Peilong Li, and Yefei Liu. "Enhancing the Performance of Evolutionary Algorithm by Differential Evolution for Optimizing Distillation Sequence." Molecules 27, no. 12 (2022): 3802. http://dx.doi.org/10.3390/molecules27123802.

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Optimal synthesis of distillation sequence is a complex problem in chemical processes engineering, which involves process structure optimization and operation parameters optimization. The study of the synthesis of distillation sequence is a crucial step toward improving the efficiency of chemical processes and reducing greenhouse gas emissions. This work introduced the concept of binary tree to encode the distillation sequence. The performance of the six evolutionary algorithms was evaluated by solving a 14-component distillation sequence synthesis problem. The best algorithm was used to optim

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44

Hartanto, Dhoni, Prima Astuti Handayani, Akhmad Sutrisno, Viona Widya Anugrahani, Asalil Mustain, and Ianatul Khoiroh. "Isopropyl Alcohol Purification through Extractive Distillation using Glycerol as an Entrainer: Technical Performances Simulation and Design." Jurnal Bahan Alam Terbarukan 8, no. 2 (2019): 133–43. http://dx.doi.org/10.15294/jbat.v8i2.23477.

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Isopropyl alcohol is widely used as industrial chemical intermediates and common solvents in households, pharmaceuticals, food, cosmetics, and medical purposes. The high purity of isopropyl alcohol requires special separation from its impurity i.e. water due to isopropyl alcohol and water form an azeotropic point, which is difficult to separate using a conventional distillation method. The azeotropic point of this mixture is at isopropyl alcohol mole fraction of 0.68 and temperature of 353.4 K. One of the optimum methods to separate an azeotrope point is through the extractive distillation whi

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45

ALAWAD, Nasir, and Afaf ALSEADY. "FUZZY CONTROLLER OF MODEL REDUCTION DISTILLATION COLUMN WITH MINIMAL RULES." Applied Computer Science 16, no. 2 (2020): 80–94. http://dx.doi.org/10.35784/acs-2020-14.

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In this paper the control of a binary distillation column is described. This control is done with fuzzy logic, one with PI- like fuzzy controller and the other with modified PI fuzzy controller, using the minimal rules for fuzzy processing. This work is focused on model reduction of Wood and Berry binary distillation column to get the best performance. It is desired to minimize the rules in order to reduce the computation time to make a faster decision. Comparisons will be made between two versions of fuzzy controllers utilizing reduced rules to verify the outputs. The controlled variables are

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46

Useche-Castelblanco, Juan Sebastián, Darío Amaya-Hurtado, and Oscar Javier Reyes-Ortiz. "Adaptive decoupling control for binary distillation column into a 3D virtual environment." Engineering review 41, no. 2 (2021): 74–86. http://dx.doi.org/10.30765/er.1480.

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The oil refinery plants have a particularly high energy consumption in the distillation process. Several authors state that these are the systems with the highest energy consumption in the petrochemical industry. Currently, work is being done on the implementation of adaptive controllers in order to improve the efficiency of the distillation process and the quality of the product. In this work the control of a binary distillation column developed within a 3D virtual laboratory is presented. Adaptive control by reference model (MRCA) is used for the manipulation of bottom and distillate concent

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47

Shimizu, K., and M. Matsubara. "Triangular decoupling for a binary distillation column under pressure control." IEEE Transactions on Automatic Control 30, no. 5 (1985): 474–77. http://dx.doi.org/10.1109/tac.1985.1103974.

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48

Wahyudi, Reza Baskara Sutapa, Ngatelan, and Budi Setiyono. "Design of Adaptive Internal Control Model on Binary Distillation Column." Journal of Physics: Conference Series 1175 (March 2019): 012104. http://dx.doi.org/10.1088/1742-6596/1175/1/012104.

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49

Anozie, A. N., F. N. Osuolale, and T. C. Aseeperi. "Exergy analysis and optimisation of binary plate distillation column operations." International Journal of Exergy 7, no. 5 (2010): 593. http://dx.doi.org/10.1504/ijex.2010.034931.

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50

Kosuge, Hitoshi, Junichi Matsudaira, Keiichi Aoki, and Koichi Asano. "Experimental approach to mass transfer in binary packed column distillation." JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 23, no. 5 (1990): 593–99. http://dx.doi.org/10.1252/jcej.23.593.

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