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Добірка наукової літератури з теми "BINARY DISTILLATION COLUMN"

Автор: Grafiati
Опубліковано: 11 вересня 2023

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Статті в журналах з теми "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 (August 31, 2022): 926–31. http://dx.doi.org/10.22214/ijraset.2022.46309.

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Анотація:
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 and perform its analysis before the distillation column is practically implemented. Distillation columns are generally considered as chemical systems, for modelling chemical systems one can use mass balance equations
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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 (June 28, 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 - tetrahydrofuran - industrial test agent (ethylene glycol (EG), dimethyl sulfoxide (DMSO), N-methylpyrrolidone (N-MP))” at 101.32 kPa. Based on the results of the evaluation of the thermodynamic criterion, DMSO and N-MP are recommended. Both agents show selective effect when separating two binary constituents. EG is selective only with respect to chloroform-tetrahydrofuran mixture. Since the tested agents show different selective effects, the final agent choice determines the qualitative composition of the product flows in the column for the extractive distillation of the three-component mixture (the first column of the flowsheet) and, accordingly, the structure of the total flowsheet. The schemes consist of two two-column complexes for extractive distillation (for the basic three-component mixture and for the binary mixture). The maximum contribution to the total reboiler energy consumption of the distillation columns is made by the first extractive distillation column: 65% (EG), 53% (N-MP) and 24% (DMSO). The use of the most selective agent reduces the energy consumption of this column: the reboiler load is maximal in the case of EG, in comparison with which the load is 47% lower in the case of N-MP and 76% lower in the case of DMSO.
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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 (February 1986): 295–304. http://dx.doi.org/10.1080/00207728608926804.

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4

Alekseev, К. А., S. M. Kirichenko, А. V. Rakov, R. А. Gaifutdinov, М. I. Farakhov, А. G. Laptev, А. N. Volkov, I. Е. Sennikov, N. V. Ledneva, and А. А. Shchepalov. "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-plate calculation of the column. The selection of the main and auxiliary equipment of the industrial vacuum distillation plant was carried out.
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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 column packings that were made of PTFE, ceramic, zirconium metal, and inox steel 316. According to the results, aqueous solutions of morpholine and acetic acid generally exhibited low relative separation efficiency (in comparison with standard mixture of heptane–methylcyclohexane), ranging between 40 % and 80 %. The highest relative efficiencies were observed with packings made of steel and ceramic. These observations will be useful for the future design of distillation columns, especially for aqueous solutions.
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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 (December 9, 2020): 85–92. http://dx.doi.org/10.6060/ivkkt.20216401.6141.

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Анотація:
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 conventional distillation column as well as a column with a heat pump and a column with heat integration were considered. As a result of the calculation experiment for each option performed using the Aspen Plus software package the optimal column parameters were determined - the total number of stages and the position of feed stage. The heat consumption in the column boiler was taken as the objective function. It is also shown that with the same characteristics of the columns, the best way to organize the process for separating the selected mixture is to compress the steam stream from rectifying profile of the column with its subsequent use in the boiler of the stripping profile according to the principle of a heat pump. It was established by a calculation experiment that heat integration by compressing steam from rectifying profile of the column and supplying it to the stripping profile gives significantly less energy saving. The calculation of internal energy saving by distillation column was carried out and it was shown that the distributed heat removal from the plates of the rectifying profile of the column and the supply of this heat to the stripping profile plates reduces internal energy saving and leads to an additional increase in heat consumption in the boiler.
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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 (December 9, 2020): 85–92. http://dx.doi.org/10.6060/ivkkt.20216401.6141.

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Анотація:
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 conventional distillation column as well as a column with a heat pump and a column with heat integration were considered. As a result of the calculation experiment for each option performed using the Aspen Plus software package the optimal column parameters were determined - the total number of stages and the position of feed stage. The heat consumption in the column boiler was taken as the objective function. It is also shown that with the same characteristics of the columns, the best way to organize the process for separating the selected mixture is to compress the steam stream from rectifying profile of the column with its subsequent use in the boiler of the stripping profile according to the principle of a heat pump. It was established by a calculation experiment that heat integration by compressing steam from rectifying profile of the column and supplying it to the stripping profile gives significantly less energy saving. The calculation of internal energy saving by distillation column was carried out and it was shown that the distributed heat removal from the plates of the rectifying profile of the column and the supply of this heat to the stripping profile plates reduces internal energy saving and leads to an additional increase in heat consumption in the boiler.
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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 (March 31, 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 (April 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 (October 17, 2022): 469–73. http://dx.doi.org/10.58571/cnca.amca.2022.088.

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Анотація:
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 results obtained show that it is possible to improve the overall performance of the distillation column, compared to traditional strategies.
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Більше джерел

Дисертації з теми "BINARY DISTILLATION COLUMN"

1

Janssen, P. W. M. "Bilinear identification of a binary distillation column." Thesis, University of Canterbury. Chemical and Process Engineering, 1986. http://hdl.handle.net/10092/7724.

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Анотація:
Low order bilinear models of chemical processes, suitable for control applications over a wide operating region, were identified. A case study on a simulated heated tank system showed that there was considerable potential for the use of bilinear models for chemical processes in which mass or energy balance equations have a bilinear structure. Bilinear models were more accurate than linear models at fitting the simulated system's behaviour over a wide range of operating points. The U-D identification algorithm used, proved to be both robust and reliable. Multi-input multi-output bilinear models of both a simulated and an experimental binary distillation column were identified using the U-D algorithm. Two factors affected the trend in the column parameters; the turn-down of the column and the shifting of the composition profile along the column. The bilinear models were good at following changes due to the turn-down, but not the large fluctuations due to changes in the composition profile. This limitation was due to the simplified liquid/vapour equilibrium relation inherent in the bilinear model, which was invalid if there were large fluctuations in composition on any of the plates.
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2

Cartwright, Peter. "Self organising knowledge based control of a binary distillation column." Thesis, Manchester Metropolitan University, 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.309885.

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3

Rajagopalan, Manoj. "Time optimal control of a high-dimensional nonlinear binary distillation column using the Luus-Jaakola optimization procedure." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 2001. http://www.collectionscanada.ca/obj/s4/f2/dsk3/ftp05/MQ62921.pdf.

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4

Khadra, Rami. "Nouvelle génération de transformateurs de chaleur, sélection de fluides de travail et optimisation des équipements du cycle en employant des technologies innovantes." Thesis, Paris, ENMP, 2015. http://www.theses.fr/2015ENMP0083.

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Ce travail contribue aux efforts de l'Union Européenne pour réduire les émissions de CO2. Son objectif est d'aider les industries produisant de la chaleur fatale à récupérer cette énergie perdue, d'augmenter sa température et de la réutiliser in situ. Les transformateurs de chaleur (Absorption Heat Transformers ou AHT), machines à absorption consommant très peu d'électricité, sont alors ici étudiés. Les AHTs existants rencontrent des problèmes comme la corrosion, la cristallisation, la toxicité et les niveaux de pression éloignés de la pression atmosphérique. Ceux-ci sont causés par les fluides conventionnels (Eau/LiBr et Ammoniaque/Eau) et s'aggravent à des températures supérieures à 120°C. Des modèles de conception ainsi que des solutions techniques, applicables avec tous mélanges de fluides organiques, sont alors proposés dans cette thèse. Ces modèles sont validés avec des données de la littérature et implémentés dans des outils d'aide à la décision.Tout d'abord, un modèle de sélection de paires de fluides organiques (parmi une liste de fluides) est développé. Les contraintes prises en compte sont, entre autres, les types et les profils de températures des sources et puits de chaleur, et les propriétés du fluide. Pour chaque type de fluide, la méthode la plus adaptée au calcul des propriétés physiques des fluides est choisie.En second lieu, pour effectuer la séparation des 2 constituants du mélange de fluides organiques, le générateur (composant recevant la chaleur fatale) et le condenseur de l'AHT sont fusionnés pour former une colonne de distillation. Un modèle d'une colonne de distillation nommée « hybride » est alors développé en adaptant la méthode de Ponchon-Savarit et en la combinant avec la méthode ETD (Equal Thermodynamic Distance). Cette colonne associe les avantages des 2 types de colonnes adiabatiques et diabatiques. Elle allie réduction de production d'entropie et meilleure exploitation des sources de chaleur à températures glissantes. La conception mécanique de la colonne hybride est aussi incluse.Troisièmement, pour atteindre la température théorique maximale du mélange de fluide déjà choisi, l'absorbeur de l'AHT (où la chaleur à haute température est libérée) est divisé en sections adiabatiques suivies par des sections diabatiques. De plus, les modèles détaillés des colonnes à bulles (fonctionnant en co-courant ou en contre-courant) ainsi que de la colonne à garnissage sont présentés et comparés entre eux.Les principaux résultats de ces travaux consistent en une nouvelle méthodologie de choix de fluides organiques pouvant remplacer les mélanges classiques surtout à températures élevées (supérieures à 130 °C). En ce qui concerne la colonne de distillation, il est montré que la colonne adiabatique constitue un meilleur choix lorsqu'une source de chaleur latente est disponible tandis qu'avec une source de chaleur sensible, la colonne hybride engendre moins de pertes exergétiques. En passant à l'absorbeur, le nouveau mode d'opération de celui-ci permet à l'utilisateur d'atteindre des températures plus élevées que celles réalisées avec les technologies actuellement disponibles. Enfin, les modèles développés permettent de choisir les technologies de distillation (adiabatique, diabatique ou hybride) et d'absorption (colonne à bulles ou à garnissage) les plus appropriées en s'adaptant à différentes problématiques industrielles
This work is part of the European union efforts to reduce its CO2 emissions. It aims to assist any waste heat producing industry in recuperating this lost thermal energy, pumping it to higher temperature levels and reusing it on site. Absorption Heat Transformers (AHT), that consume little electricity, are used for this task. Current AHT problems such as corrosion, crystallization, toxicity and inconvenient pressure levels are caused by conventionally used H2O/LiBr and NH3/ H2O working fluids and get worse at temperatures exceeding 120°C. Potential solutions are thus suggested. According to them, models are developed; they are all able to operate with any organic mixture and are customized to accompany the industrialist from start to finish. These solutions were validated by comparing them with literature data and are implemented into several tools.Firstly, a model selects the optimal organic binary mixture -among a list of fluids- in terms of the real case application's constraints: Heat transfer fluids used, Heat source's and heat sink's types and temperature profiles, mixtures transport properties among other parameters. Suitable thermodynamic model is selected for different fluid group types.Secondly, in order to separate the 2 components of the chosen mixture of organic compounds, the AHT generator (component which receives waste heat) is merged with the AHT condenser thus forming a distillation column. A “hybrid column” is designed by modifying the Ponchon-Savarit method and combining it with the Equal Thermodynamic Distance (ETD) method. This new column associates the best features of the two columns. It reduces entropy production rates and best exploits temperature gliding heat sources. Mechanical design for the hybrid column is also included.Thirdly, to ensure that the maximum theoretical temperature of the working fluid is reached, the AHT absorber (where high temperature heat is released) is divided into consecutive adiabatic parts followed by diabatic ones. Detailed Models for co-current and counter-current bubble columns as well as packing columns are presented and compared.Main results consist in a selection methodology of organic compounds mixtures, capable of replacing conventional ones specially at temperatures higher than 130 °C. It's also shown that adiabatic columns are better options when latent type heat sources are available while hybrid columns lose less exergy when used with sensible heat sources. As for the absorber, the new operating mode provides the user with higher temperatures than currently reached by available technologies. Finally, using the developed models, tailored and most suitable distillation (adiabatic, diabatic or hybrid columns) and absorber (bubble or packing columns) technologies can be proposed depending on the industrial specific cases and requirements
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5

Peng, Chi-Chun, and 彭棋俊. "Windows Programming of Binary Distillation Column under Atmospheric Pressure." Thesis, 2012. http://ndltd.ncl.edu.tw/handle/mfb8d7.

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Анотація:
碩士
國立臺北科技大學
化學工程研究所
100
The distillation column is a common and important operation unit in the chemical industry. The process utilizes the difference of the boiling point to separate the components. The aim of this research is to develop a program can simulate the steady state of distillation column for different number of stage, feed tray location, flow rate of feed, reflux rate, heat duty. In addition, the dynamic control simulation is also provided. Microsoft Visual Basic 2010 was used to develop the program. The subprograms for solving the mass balance, energy balance and phase equilibrium equations was constructed firstly. Two temperature control loops were added into the fully program. By virtue of the simulation examples, the steady state data is similar to references and the dynamic response is also reasonable. Therefore this simulation program can be provided for further studies and research.
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6

Li, Kuan-Min, and 李冠旻. "Windows Programming of Binary Batch Distillation Column under Atmospheric Pressure." Thesis, 2013. http://ndltd.ncl.edu.tw/handle/gqc932.

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Анотація:
碩士
國立臺北科技大學
化學工程研究所
101
Batch Distillation is an important process in chemical industry. Batch distillation is often used to produce small amounts of products with high added value. Most of textbooks focus on the steady state. However, the dynamics operation is more important. 　　The research developed a windows program for binary batch distillation column under atmospheric pressure by Visual Basic 2010. The subprograms for solving the mass balance, energy balance and phase equilibrium equations were constructed firstly. Three strategies for operating the distillate flow rate were applied in the program. By simulation examples, different operation strategies have the different optimal control conditions; the program can apply the capability for user to learn the dynamic operations of batch distillation.
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7

Mishra, Rakesh Kumar. "Design of an Internal Model Controller for Binary Distillation Column." Thesis, 2013. http://ethesis.nitrkl.ac.in/4812/1/211EC3314.pdf.

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In this report Internal Model Control, Lead- Lag based Internal Model Control and modified Internal Model Control for distillation column has been proposed. The prime objective of any industrial process is to perform efficiently with optimum cost reduction. Internal Model Control (IMC) is a commonly used technique that provides a transparent mode for the designing and easy tuning of control structure . I have designed the internal model control for binary distillation column .The transfer function has been taken from Wood and Berry model. The internal model control has been designed considering three strategies namely, process perfect, process mismatch with disturbances and process model with considering only disturbance. It has also been tried to reduce the disturbance created in the system by varying tuning parameter (ë). In the second proposal, Lead-Lag based Internal Model Control method is proposed based on Internal Model Control (IMC) strategy. We have also designed the Lead-Lag based Internal Model Control for binary distillation column. We have found the composition control and disturbance rejection using Lead-Lag based IMC and comparing with the response of generalize Internal Model Controller. Finally we have design the Modified Internal Model Structure, and find the response for binary distillation column and compare with generalize Internal Model Controller response. This thesis presents an Internal Model Control, lead- lag based internal model control and modified internal model control strategy for binary distillation column and comparing the response with each other. The aim is to provide a best strategy to control the distillation column that is favourable in terms of industrial implementation. I have used matlab software to simulate the all process.
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Книги з теми "BINARY DISTILLATION COLUMN"

1

Brydon, D. A. Neural network modelling of a binary distillation column. Manchester: UMIST, 1994.

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2

Rajagopalan, Manoj. Time optimal control of a high-dimensional, nonlinear binary distillation column using the Luus-Jaakola optimization procedure. Ottawa: National Library of Canada, 2001.

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3

Edwards, J. B. Interpretation and utilization of Parametric Models of Binary distillation Columns: Relating plant and control design. Sheffield: University of Sheffield, Dept. of Automatic Control and Systems Engineering, 1995.

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Частини книг з теми "BINARY DISTILLATION COLUMN"

1

Gálvez, Akemi, and Andrés Iglesias. "Binary Distillation Column Design Using Mathematica." In Lecture Notes in Computer Science, 848–57. Berlin, Heidelberg: Springer Berlin Heidelberg, 2003. http://dx.doi.org/10.1007/3-540-44860-8_88.

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2

Singh, Amit Kumar, H. P. Singh, and Sachin Mishra. "Validation of ANN-Based Model for Binary Distillation Column." In Proceeding of International Conference on Intelligent Communication, Control and Devices, 235–42. Singapore: Springer Singapore, 2016. http://dx.doi.org/10.1007/978-981-10-1708-7_27.

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3

Mishra, Rakesh Kumar, and Tarun Kumar Dan. "Design of Lead-Lag Based Internal Model Controller for Binary Distillation Column." In Advancements of Medical Electronics, 207–14. New Delhi: Springer India, 2015. http://dx.doi.org/10.1007/978-81-322-2256-9_19.

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4

de Canete, Javier Fernandez, Alfonso Garcia-Cerezo, Inmaculada Garcia-Moral, Pablo del Saz, and Ernesto Ochoa. "Object-Oriented Neurofuzzy Modeling and Control of a Binary Distillation Column by Using MODELICA." In Engineering Applications of Neural Networks, 51–60. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-32909-8_6.

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5

Vagi, F., R. K. Wood, A. J. Morris, and M. Tham. "MULTIVARIABLE SELF-TUNING CONTROL OF A BINARY DISTILLATION COLUMN." In Digital Computer Applications to Process Control, 207–15. Elsevier, 1986. http://dx.doi.org/10.1016/b978-0-08-032554-5.50029-x.

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6

Broll, J., and H. Gelbe. "FEEDFORWARD/FEEDBACK CONTROL OF A BINARY HIGH PURITY DISTILLATION COLUMN." In Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes, 237–42. Elsevier, 1993. http://dx.doi.org/10.1016/b978-0-08-041711-0.50039-8.

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7

Pullinen, R., P. Pietilä, T. Jussila, and P. Lautala. "A COMPARATIVE STUDY OF LINEAR AND NONLINEAR MULTIVARIABLE BINARY DISTILLATION COLUMN CONTROL." In Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes, 231–36. Elsevier, 1993. http://dx.doi.org/10.1016/b978-0-08-041711-0.50038-6.

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8

Chai, T. Y., and G. Wang. "APPLICATION OF A NEW MULTIVARIABLE ADAPTIVE DECOUPLING CONTROLLER TO A BINARY DISTILLATION COLUMN." In Advanced Control of Chemical Processes 1991, 71–76. Elsevier, 1992. http://dx.doi.org/10.1016/b978-0-08-041267-2.50017-6.

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9

Castro, R., J. Alvarez, and G. Bornard. "A DISTURBANCE DECOUPLING CONTROL LAW WITH OUTPUT DYNAMIC MATCHING FOR NONLINEAR SYSTEMS. APPLICATION TO A BINARY DISTILLATION COLUMN." In Simulation of Control Systems, 193–98. Elsevier, 1987. http://dx.doi.org/10.1016/b978-0-08-034349-5.50037-8.

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10

Aharchi, Moussa, Nbigui Taibi, and Allam Fouad. "Effect of Feed Quality on the Internal Reflux and Boil-Up Ratios of a Binary Continuous Distillation Column." In 1ST INTERNATIONAL CONFERENCE ON PHYSICAL AND ENGINEERING SCIENCES (ICPES’22), 119–25. Sciendo, 2023. http://dx.doi.org/10.2478/9788367405249-020.

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Тези доповідей конференцій з теми "BINARY DISTILLATION COLUMN"

1

Gálvez, Akemi, and Andrés Iglesias. "Designing a Distillation Column for Binary Mixtures." In Proceedings of the Fifth International Mathematica Symposium. PUBLISHED BY IMPERIAL COLLEGE PRESS AND DISTRIBUTED BY WORLD SCIENTIFIC PUBLISHING CO., 2003. http://dx.doi.org/10.1142/9781848161313_0009.

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2

Adel, Islam Mohamed, Irraivan Elamvazuthi, and Noor Hazrin Hany Binti Mohd Hanif. "Monitoring and controlling system for binary distillation column." In 2009 IEEE Student Conference on Research and Development (SCOReD). IEEE, 2009. http://dx.doi.org/10.1109/scored.2009.5442975.

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3

Drgona, Jan, Zdenko Takac, Milan Hornak, Richard Valo, and Michal Kvasnica. "Fuzzy control of a laboratory binary distillation column." In 2017 21st International Conference on Process Control (PC). IEEE, 2017. http://dx.doi.org/10.1109/pc.2017.7976200.

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4

"Design of Control Structure for Binary Distillation Column." In 3rd International Conference on Advances in Engineering Sciences and Applied Mathematics. International Institute of Engineers, 2015. http://dx.doi.org/10.15242/iie.e0315071.

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5

Khelassi, Abdelmadjid, Riad Bendib, and Abdelhai Benhalla. "Configurations of binary distillation column for optimal control." In 2012 UKACC International Conference on Control (CONTROL). IEEE, 2012. http://dx.doi.org/10.1109/control.2012.6334731.

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6

Diaz, S., J. R. Perez-Correa, Aldo Cipriano, and M. Fernandez-Fernandez. "Intelligent control applications on a binary distillation column." In 2016 IEEE International Conference on Automatica (ICA-ACCA). IEEE, 2016. http://dx.doi.org/10.1109/ica-acca.2016.7778496.

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7

ODIN, ANTONIO TORRENTS, and MATILDE SANTOS. "FUZZY CONTROL APPROACH OF A BINARY DISTILLATION COLUMN." In Proceedings of the 9th International FLINS Conference. WORLD SCIENTIFIC, 2010. http://dx.doi.org/10.1142/9789814324700_0048.

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8

Singh, Amit Kumar, Barjeev Tyagi, and Vishal kumar. "Fuzzy rule-based controller for binary distillation column." In the International Conference. New York, New York, USA: ACM Press, 2011. http://dx.doi.org/10.1145/2007052.2007086.

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9

Yadav, Vikas, Vritank Yadav, Amar Nath Jha, Sarthak Tanwar, and Nishant Singh. "PID Control using Metaheuristics for Binary Distillation Column." In 2023 International Conference on Recent Advances in Electrical, Electronics & Digital Healthcare Technologies (REEDCON). IEEE, 2023. http://dx.doi.org/10.1109/reedcon57544.2023.10150966.

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10

Kale, Shashikant R., and Sudhir D. Agashe. "Performance enhancement of Binary Batch Distillation Column Pilot Plant." In 2014 International Conference on Control, Instrumentation, Communication and Computational Technologies (ICCICCT). IEEE, 2014. http://dx.doi.org/10.1109/iccicct.2014.6992984.

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