Academic literature on the topic 'BINARY DISTILLATION COLUMN'

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Journal articles on the topic "BINARY DISTILLATION COLUMN"

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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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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