Relevant bibliographies by topics / Batch distillation column

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  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers

Academic literature on the topic 'Batch distillation column'

Author: Grafiati
Published: 4 June 2021
Last updated: 6 February 2022

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Journal articles on the topic "Batch distillation column"

1

Diwekar, Urmila M., and K. P. Madhavan. "Multicomponent batch distillation column design." Industrial & Engineering Chemistry Research 30, no. 4 (April 1991): 713–21. http://dx.doi.org/10.1021/ie00052a014.

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Noda, Masaru, Akifumi Kato, Shinji Hasebe, and Iori Hashimoto. "Optimal structure of batch distillation column." Computers & Chemical Engineering 23 (June 1999): S105—S108. http://dx.doi.org/10.1016/s0098-1354(99)80027-1.

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3

Hawaidi, Ebrahim Ali Mohamed, Mustafa T. Yagub, and Riyad Ageli Saleh. "ACETONE RECOVERY USING BATCH DISTILLATION." Scientific Journal of Applied Sciences of Sabratha University 2, no. 2 (September 27, 2019): 82–98. http://dx.doi.org/10.47891/sabujas.v2i2.82-98.

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This study focuses on determining the feasibility of obtaining maximum mole percentage of acetone (99 mole%) in the distillate stream from a 3 mole% acetone waste stream using batch distillation. The device which is used in this work has eight trays that will act as the stages of the batch distillation. The effects of varying reflux ratio and heat load (power) on acetone concentration were studied. Moreover, the operating conditions for the bath distillation column such as flooding and weeping with the extreme limits of operation were considered. The temperatures were also be recorded at each tray. The McCabe-Thiele method was used to determine the theoretical number of trays and compared with actual trays (column efficiency). For a chemical analysis of acetone/water compositions a refractometer was used for a chemical analysis, known acetone/water concentrations were analysed and used to construct a calibration curve. The results obtained showed that, the acetone concentration increases with increasing reflux ratio until a highest concentration was reached. Then, the concentration gradually decreases with increasing reflux ratio. However, the distillate stream with 99 mole % acetone was achieved at a reflux ratio of R=3 and at both powers 0.5 kw and 0.7 kw. Finally, the highest overall column efficiency reached by this work was about 75%.
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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 (December 1, 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 requires from 4.00 to 34.67% more time to complete a given separation. The elimination of the vapor bypass in the multivessel column is impractical though it has a positive effect on the batch time requirements. Thus, the multivessel column, with the vapor stream bypassing the intermediate vessel, is proposed as the best candidate for a binary zeotropic mixture with low concentration of light component, low relative volatility and high product purity demand. Furthermore, an experimental multivessel column with vapor bypass is built and the corresponding experiments verify the simulations.
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Rohman, Arief Syaichu, Pranoto Hidaya Rusmin, Renny Maulidda, Egi Muhammad Idris Hidayat, Carmadi Machbub, and Dimitri Mahayana. "Modelling of the Mini Batch Distillation Column." International Journal on Electrical Engineering and Informatics 10, no. 2 (June 30, 2018): 350–68. http://dx.doi.org/10.15676/ijeei.2018.10.2.11.

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Bahar, Almιla, and Canan Özgen. "State Estimation for a Reactive Batch Distillation Column." IFAC Proceedings Volumes 41, no. 2 (2008): 3304–9. http://dx.doi.org/10.3182/20080706-5-kr-1001.00561.

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Denes, F., P. Lang, G. Modla, and X. Joulia. "New double column system for heteroazeotropic batch distillation." Computers & Chemical Engineering 33, no. 10 (October 2009): 1631–43. http://dx.doi.org/10.1016/j.compchemeng.2009.01.011.

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Tang, Ke, and Peng Bai. "Cascaded Columns of Total Reflux Batch Distillation with Periodic Liquid Exchange." Advanced Materials Research 690-693 (May 2013): 1495–99. http://dx.doi.org/10.4028/www.scientific.net/amr.690-693.1495.

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A new type of operation mode of cascaded columns of total reflux batch distillation with periodic liquid exchange was proposed. The feasibility of the new operation, which is suitable for separations of mixtures of close boiling point, thermo-sensitive material and isotopes, was proved by the experiments in which two columns and three columns in periodic liquid exchange were used with ethanol-isopropanol, ethylbenzene- paraxylene as the experimental mixtures. The results indicate that the new operation mode can generate summation effect of theoretical plates by periodic liquid exchange between columns, while the total pressure drop is the same as that of a single column.
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Lukács, T., C. Stéger, E. Rév, M. Meyer, and Z. Lelkes. "Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column." International Journal of Chemical Engineering 2011 (2011): 1–16. http://dx.doi.org/10.1155/2011/231828.

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A general overall feasibility methodology of batch reactive distillation of multireaction systems is developed to study all the possible configurations of batch reactive distillation. The general model equations are derived for multireaction system with any number of chemical equilibrium-limited reactions and for any number of components. The present methodology is demonstrated with the detailed study of the transesterification of dimethyl carbonate in two reversible cascade reactions in batch reactive distillation process. Pure methanol is produced as distillate, and pure diethyl carbonate is produced at the bottom simultaneously in middle-vessel column; in each section, continuous feeding of ethanol is necessary. The results of feasibility study are successfully validated by rigorous simulations.
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Hao, Wenfeng. "A Short-Cut Design Technique to Batch Distillation Column." Advances in Chemical Engineering and Science 09, no. 03 (2019): 263–79. http://dx.doi.org/10.4236/aces.2019.93020.

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Dissertations / Theses on the topic "Batch distillation column"

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Dénes, Ferenc. "New Double-Column Systems for Batch Heteroazeotropic Distillation." Thesis, Toulouse, INPT, 2012. http://www.theses.fr/2012INPT0124/document.

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J'ai étudié deux nouvelles configurations de double-colonne pour distillation hétéroazéotropique. Ces configurations sont appropriées à la récupération simultanée des composants des mélanges binaires hétéroazéotropiques et homoazéotropiques (en utilisant un tiers corps (entraîneur)). Elle sont opérées en système fermé, c'est-à-dire, il n'y a pas de soutirage de produit continu. D'abord, en appliquant un modèle simplifié, j'ai étudié la faisabilité de la séparation d'un mélange hétéroazéotropique (1-butanol – eau), puis celle d'un mélange homoazéotropique (2-propanol – eau) aidé par entraîneur benzène ou cyclohexane, en utilisant le SDC. Puis, j'ai étudié cette configuration par modélisation rigoureuse, en appliquant le simulateur dynamique du logiciel professionnel ChemCAD (CC-DColumn). J'ai comparé la nouvelle configuration avec le RD, sur la base des résultats obtenus par toutes les deux méthodes d'étude. Le SDC s'est avéré faisable et compétitif avec le RD : pendant la même durée ou plus courte, les rendements des composants ont été plus élevés. Puis, on a étendu le SDC à un système plus flexible (système de double-colonne généralisé, SDCG) qui est approprié à la séparation des mélanges binaires homoazéotropiques aidé par entraîneur (en le cas présent : cyclohexane ou n-hexane). J'ai étendu la méthode de faisabilité aussi à l'étude de cette configuration. Le SDCG s'est avéré aussi faisable. En appliquant modélisation rigoureuse, j'ai étudié les effets des nouveaux paramètres opératoires sur la durée, et j'ai comparé le DCG avec le SDC. Le SDCG s'est avéré encore plus avantageux que le SDC : la durée a été plus courte, et les besoins spécifiques d'énergie des produits ont été plus bas. J'ai étudié le SDC et le SDCG aussi par des manipulations exécutées sur installations de taille laboratoire et pilote. D'abord, j'ai fait des manipulations laboratoires pour la séparation du mélange binaire hétéroazéotropique, en utilisant une installation en verre qui a été opérée aussi comme RD et SDC. Le SDC s'est avéré faisable et compétitif avec le RD aussi sur la base des résultats de ces manipulations : pendant la même durée, les rendements des tous les deux composants ont été plus élevés. Puis, en utilisant l'installation pilote comme SDC, j'ai étudié la séparation ci-dessus. Après cette manipulation, j'ai étudié la séparation du mélange binaire homoazéotropique en appliquant n-hexane comme entraîneur, en opérant le système comme RD et SDCG. La manipulation faite avec le SDCG a montré que la production simultanée de deux composants est faisable avec cette configuration
Distillation is the method the most frequently applied for the separation of liquid mixtures, e.g. for the recovery of the components of the waste solvent mixtures. Because of the high energy demand of these processes the optimal design and operation of the distillation equipments are important from economic and also environmental points of view. The separation of the azeotropic mixtures needs special distillation methods like heteroazeotropic distillation. In the pharmaceutical and fine chemical industries it is often applied in batch mode. The aims of the thesis are to study the feasibility of a new Double-Column System (DCS) for batch heteroazeotropic distillation and to compare it with the traditional Batch Rectifier (BR) equipped with a decanterto study the above configurations by rigorous simulationto extend the DCS (Generalised Double-Column System, GDCS) and to study this new configuration by the above methodsto do laboratory experiments for both configurations in order to prove the feasibility of the separation and validate the calculations, respectively. Two new double-column configurations for batch heteroazeotropic distillation were studied. These configurations are designed to produce simultaneously the components of binary heteroazeotropic and homoazeotropic mixtures (by using an entrainer). They are operated in closed system (without continuous product withdrawal). First the feasibility of the separation of a heteroazeotropic mixture (1-butanol – water) and that of a homoazeotropic one by using an entrainer (isopropanol – water + benzene or cyclohexane) in the DCS were investigated by a simplified model. Then the operation of this configuration was modelled by rigorous simulation by using the dynamic simulator of the professional flowsheet simulator ChemCAD (CC-DColumn). On the basis of the results obtained by both methods the new configuration was compared with the BR. The DCS proved to be feasible and competitive with the BR: during the same or shorter time the recoveries of the components were higher. Then the DCS was extended to a more flexible version (Generalised Double-Column System, GDCS), which is suitable for the separation of binary homoazeotropic mixtures (by using an entrainer, in this work: cyclohexane or n- exane). The feasibility method was extended for the study of this configuration, as well. The GDCS proved to be feasible. Then the effects of its additional operational parameters on the duration were studied by rigorous simulation. The GDCS was compared with the DCS by rigorous simulation, as well. The GDCS proved to be more advantageous than the DCS: the duration was shorter and the specific energy demands of the products were lower. The DCS and GDCS were also investigated by laboratory and pilot plant experiments. First laboratory experiments were done for the separation of the binary heteroazeotropic mixture in a simple small size glass equipment operated as BR and DCS. The DCS proved to be feasible and competitive with the BR also on the basis of the results of these experiments: during the same time the recovery of both components were higher. Then a pilot plant was used for the same separation as a DCS. After this experiment the separation of the binary homoazeotropic mixture by using n-hexane as entrainer was studied in the equipment operated as BR and GDCS. The experiment showed that the simultaneous production of two components is feasible also in the GDCS
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Yildiz, Ugur. "Multicomponent Batch Distillation Column Simulation And State Observer Design." Master's thesis, METU, 2002. http://etd.lib.metu.edu.tr/upload/12605551/index.pdf.

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In the control of batch and continuous distillation columns, one of the most challenging problem is the difficulty in measuring compositions. This problem can be handled by estimating the compositions from readily available online temperature measurements using a state observer. The aim of this study is to design a state observer that estimates the product composition in a multicomponent batch distillation column (MBDC) from the temperature measurements and to test this observer using a batch column simulation. To achieve this, first a model for MBDC is prepared and compared with the data from literature where a case column is utilized. After checking the validity of the simulation package, it is used as a fictitious process for the performance evaluations. In the second phase of the study, an extended Kalman Filter (EKF) is designed by utilizing a simplified model of MBDC and it is implemented for performance investigation on the case column with 8 trays separating the mixture of cyclohexane, n-heptane and toluene. The simplified model utilized in EKF results in response, which have some deviation with rigorous model, mainly due to the simplification of vapor-liquid equilibrium relationship. In the performance evaluation, the tuning parameters of EKF
the diagonal terms of process noise covariance matrix and the diagonal terms of measurement model noise covariance matrix are changed in the range of 50¡
1x10¡
7 and 0:5¡
5x108 and the optimum values are found as 0:00001 and 5000, respectively. The effect of number of measurement points is also investigated with a result of number of component measurements. The effect of measurement period value is also studied and found that it has a major effect on the performance which has to be determined by the available computational facilities. The control of the column is done by utilizing the designed EKF estimator and the estimator is successfully used in controlling the product purities in MBDC under variable reflux-ratio operation.
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Bahar, Almila. "Modeling And Control Studies For A Reactive Batch Distillation Column." Phd thesis, METU, 2007. http://etd.lib.metu.edu.tr/upload/12608344/index.pdf.

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Modeling and inferential control studies are carried out on a reactive batch distillation system for the esterification reaction of ethanol with acetic acid to produce ethyl acetate. A dynamic model is developed based on a previous study done on a batch distillation column. The column is modified for a reactive system where Artificial Neural Network Estimator is used instead of Extended Kalman Filter for the estimation of compositions of polar compounds for control purposes. The results of the developed dynamic model of the column is verified theoretically with the results of a similar study. Also, in order to check the model experimentally, a lab scale column (40 cm height, 5 cm inner diameter with 8 trays) is used and it is found that experimental data is not in good agreement with the models&rsquo
. Therefore, the model developed is improved by using different rate expressions and thermodynamic models (fi-fi, combination of equations of state (EOS) and excess Gibbs free energy (EOS-Gex), gama-fi) with different equations of states (Peng Robinson (PR) / Peng Robinson - Stryjek-Vera (PRSV)), mixing rules (van der Waals / Huron Vidal (HV) / Huron Vidal Original (HVO) / Orbey Sandler Modification of HVO (HVOS)) and activity coefficient models (NRTL / Wilson / UNIQUAC). The gama-fi method with PR-EOS together with van der Waals mixing rule and NRTL activity coefficient model is selected as the best relationships which fits the experimental data. The thermodynamic models
EOS, mixing rules and activity coefficient models, all are found to have very crucial roles in modeling studies. A nonlinear optimization problem is also carried out to find the optimal operation of the distillation column for an optimal reflux ratio profile where the maximization of the capacity factor is selected as the objective function. In control studies, to operate the distillation system with the optimal reflux ratio profile, a control system is designed with an Artificial Neural Network (ANN) Estimator which is used to predict the product composition values of the system from temperature measurements. The network used is an Elman network with two hidden layers. The performance of the designed network is tested first in open-loop and then in closed-loop in a feedback inferential control algorithm. It is found that, the control of the product compositions with the help of an ANN estimator with error refinement can be done considering optimal reflux ratio profile.
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Ceylan, Hatice. "Control And Simulation Studies For A Multicomponent Batch Packed Distillation Column." Master's thesis, METU, 2007. http://etd.lib.metu.edu.tr/upload/12608688/index.pdf.

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During the last decades, batch distillation is preferably used with an increasing demand over continuous one, to separate fine chemicals in chemical and petroleum industries, due to its advantages like, flexibility and high product purity. Consequently, packed distillation columns, with newly generated packing materials, are advantageous compared to plate columns because of their smaller holdups, resistivity to corrosive materials and their higher separation efficiencies. Also, in many industrial applications, mathematical models of distillation systems are frequently used in order to design effective control systems, to train operating personnel and to handle fault diagnostics. Thus, the main objective of this study is to develop a mathematical model for a multicomponent batch distillation column, which is used to separate mixtures at low operating pressures, packed with random packing materials. In multicomponent batch packed distillation, operation with optimum reflux ratio profile is important for efficiency to maximize the amount of the distillate with a specified concentration, for a given time. Therefore, it is also aimed to find the optimum reflux ratio profile for the multicomponent batch packed distillation column. A simulation algorithm is written with the aid of MATLAB and FORTRAN programming languages by taking into account pressure drop and variation of physical properties. The selected incremental bed height, &
#916
z, to be used in the simulation program has an effect on the accuracy of the results. This is analyzed and the optimal incremental height is found to be 3.5 cm for a 1.5m bed height. The change in distillate compositions with a given constant reflux ratio is found to be similar with those of previous studies. The simulation code is also used to obtain responses in distillate compositions for different reflux ratios, condenser holdups and reboiler duties and compared with similar studies found from literature and found to be adequate. Finally, experiments are conducted to verify simulation algorithm by using a lab-scale packed distillation column for the separation of a polar mixture of ethanol and water. It is observed that, there is a good agreement between the experimental and simulation results. After the verification of dynamic model, optimum operation policy to maximize product amount is investigated numerically by using capacity factor approach. The column is operated with and without recycling of the holdups of the slop cut tanks, in order to examine the effect of recycling on capacity factor, CAP. It is observed that, recycling of the molar holdups of the slop cut tanks is resulted in a 28% increase in the separation efficiency.
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Shah, Azam. "Neural network minimum entropy modelling and control of a batch distillation column." Thesis, University of Manchester, 2009. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.508522.

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Safdarnejad, Seyed Mostafa. "Developing Modeling, Optimization, and Advanced Process Control Frameworks for Improving the Performance of Transient Energy-Intensive Applications." BYU ScholarsArchive, 2016. https://scholarsarchive.byu.edu/etd/6057.

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The increasing trend of world-wide energy consumption emphasizes the importance of ongoing optimization of new and existing technologies. In this dissertation, two energy–intensive systems are simulated and optimized. Advanced estimation, optimization, and control techniques such as a moving horizon estimator and a model predictive controller are developed to enhance the profitability, product quality, and reliability of the systems. An enabling development is presented for the solution of complex dynamic optimization problems. The strategy involves an initialization approach to large–scale system models that both enhance the computational performance as well as the ability of the solver to converge to an optimal solution. One particular application of this approach is the modeling and optimization of a batch distillation column. For estimation of unknown parameters, an L1-norm method is utilized that is less sensitive to outliers than a squared error objective. The results obtained from the simple model match the experimental data and model prediction for a more rigorous model. A nonlinear statistical analysis and a sensitivity analysis are also implemented to verify the reliability of the estimated parameters. The reduced–order model developed for the batch distillation column is computationally fast and reasonably accurate and is applicable for real time control and online optimization purposes. Similar to estimation, an L1-norm objective function is applied for optimization of the column operation. Application of an L1-norm permits explicit prioritization of the multi–objective problems and adds only linear terms to the problem. Dynamic optimization of the column results in a 14% increase in the methanol product obtained from the column with 99% purity. In a second application of the methodology, the results obtained from optimization of the hybrid system of a cryogenic carbon capture (CCC) and power generation units are presented. Cryogenic carbon capture is a novel technology for CO2 removal from power generation units and has superior features such as low energy consumption, large–scale energy storage, and fast response to fluctuations in electricity demand. Grid–level energy storage of the CCC process enables 100% utilization of renewable power sources while 99% of the CO2 produced from fossil–fueled power plants is captured. In addition, energy demand of the CCC process is effectively managed by deploying the energy storage capability of this process. By exploiting time–of–day pricing, the profit obtained from dynamic optimization of this hybrid energy system offsets a significant fraction of the cost of construction of the cryogenic carbon capture plant.
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Furlonge, Haydn Ian. "Optimal operation of unconventional batch distillation columns." Thesis, Imperial College London, 2000. http://hdl.handle.net/10044/1/8078.

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Cesur, Serap. "Study of modelling, simulation and different operation modes and control for packed batch distillation columns." Thesis, University of Bath, 1993. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.332843.

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Mehlhorn, Arndt. "Modelización avanzada de columnas de destilación de operación discontinua." Doctoral thesis, Universitat Politècnica de Catalunya, 1998. http://hdl.handle.net/10803/6448.

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La tesis doctoral se compone de dos partes fundamentales: El desarrollo teórico de un modelo de simulación para la destilación discontinua y la validación de este mediante experimentos hechos en una planta piloto de destilación discontinua.
La parte teórica se divide en la parte de desarrollo del modelo y en la parte de la implementación del modelo en un programa de simulación. El nuevo modelo desarrollado es un modelo de transferencia de materia que se distingue de los desarrollos anteriores por su capacidad de contemplar la cinética de la transferencia de materia tal como la hidrodinámica. La incorporación de efectos hidrodinámicos se basa principalmente en la observación de diferentes geometrías de contacto en una columna de platos perforados. Estas geometrías de contacto son canales de vapor y burbujas. En caso de las burbujas se distingue entre grandes y pequeñas con diferentes propiedades hidrodinámicas. De esta forma el modelo contempla tres diferentes clases de vapor, dos clases de vapor de desequilibrio y una de equilibrio (burbujas pequeñas). Para las clases de vapor de desequilibrio se calcula explícitamente los caudales de materia que traviesen la interfase basándose en la teoría de Maxwell-Stefan de transferencia de materia multicomponente.
La parte experimental se divide en la parte de diseño de la columna usada en una planta piloto y en la de la realización de los experimentos. El diseño de la columna tiene como objetivo la obtención de un medio de validación del nuevo modelo desarrollado. Por tanto está equipado con un gran número de sensores de temperatura, de presión y de tomas de muestra. También la realización de los experimentos se adapta al fin de la validación del modelo, ya que la frecuencia de toma de muestra y de capturación de señales de temperatura es elevada.
La memoria de la tesis contiene una comparación amplia de los resultados experimentales con los de la simulación. Estas comparaciones demuestran una determinada superioridad del modelo desarrollado sobre desarrollos anteriores.
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Aqar, Dhia Y. "Modelling and Optimization of Conventional and Unconventional Batch Reactive Distillation Processes. Investigation of Different Types Batch Reactive Distillation Columns for the Production of a Number of Esters such as Methyl Lactate, Methyl Decanoate, Ethyl Benzoate, and Benzyl Acetate using gPROMS." Thesis, University of Bradford, 2018. http://hdl.handle.net/10454/17139.

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The synthesis of a number of alkyl esters such as methyl lactate, methyl decanoate, and ethyl benzoate via esterification in a reactive distillation is quite challenging. It is due to the complexity in the thermodynamic behaviour of the chemical species in the reaction mixture in addition to the difficulty of keeping the reactants together in the reaction section. One of the reactants (in these esterification reactions) having the lowest boiling point can separate from the other reactant as the distillation continues. This can result in a significant drop in the reaction conversion in a conventional reactive distillation whether it is a batch or a continuous column. To overcome this challenge, new different types of batch reactive distillation column configurations: (1) integrated conventional (2) semi-batch (3) integrated semi-batch (4) integrated dividing-wall batch distillation columns have been proposed here. Four esterification reaction schemes such as (a) esterification of lactic acid (b) esterification of decanoic acid (c) esterification of benzoic acid (d) esterification of acetic acid are investigated here. A detailed dynamic model based on mass, energy balances, chemical reaction, and rigorous thermodynamic (chemical and physical) properties is considered and incorporated in the optimisation framework within gPROMS (general PROcess Modelling System) software. It is found that for the methyl lactate system, the i-SBD operation outperforms the classical batch operations (CBD or SBD columns) to satisfy the product constraints. While, for the methyl decanoate system, the i-DWCBD operation outperforms all CBD, DWBD and sr-DWBD configurations by achieving the higher reaction conversion and the maximum product purity. For the ethyl benzoate system, the performance of i-CBD column is superior to the CBD process in terms of product quality, and conversion rate of acid. The CBD process is found to be a more attractive in terms of operating time saving, and annual profit improvement compared to the IBD, and MVD processes for the benzyl acetate system.
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Books on the topic "Batch distillation column"

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E, Rijnsdorp John, International Federation of Automatic Control. Working Group on Chemical Process Control., and European Federation of Chemical Engineering., eds. Dynamics and control of chemical reactors, distillation columns, and batch processes: Selected papers from the IFAC Symposium, Maastricht, the Netherlands, 21-23 August 1989. Oxford, England: Published for the International Federation of Automatic Control by Pergamon Press, 1990.

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Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes. Elsevier, 1993. http://dx.doi.org/10.1016/c2009-0-00257-8.

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Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes (Dycord'95). Elsevier, 1995. http://dx.doi.org/10.1016/c2009-0-00861-7.

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(Editor), J. E. Rijnsdorp, J. F. Macgregor (Editor), B. D. Tyreus (Editor), and T. Takamatsu (Editor), eds. Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes (DYCORD+'89) (IFAC Symposia Series). Pergamon, 1990.

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Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes (DYCORD+'89) (IFAC Symposia Series). Pergamon, 1990.

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G, Balchen Jens, International Federation of Automatic Control., and IFAC Symposium on Dynamics and Control of Chemical Reactors, Distillation Columns, and Batch Processes (3rd : 1992 : University of Maryland), eds. Dynamics and control of chemical reactors, distillation columns, and batch processes (DYCORD+ '92): Selected papers from the 3rd IFAC symposium, Maryland, USA, 26-29 April 1992. Oxford: Published for the International Federation of Automatic Control by Pergamon Press, 1993.

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Dynamics and control of chemical reactors, distillation columns, and batch processes (DYCORD+ '95): A postprint volume from the 4th IFAC Symposium, Helsingør, Denmark, 7-9 June 1995. Oxford, UK: Published for the International Federation of Automatic Control by Pergamon Press, 1995.

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Book chapters on the topic "Batch distillation column"

1

Nitsche, M., and R. Gbadamosi. "Discontinuous Batch Distillation." In Practical Column Design Guide, 165–85. Cham: Springer International Publishing, 2017. http://dx.doi.org/10.1007/978-3-319-51688-2_6.

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"COLUMN CONFIGURATIONS." In Batch Distillation, 11–16. PUBLISHED BY IMPERIAL COLLEGE PRESS AND DISTRIBUTED BY WORLD SCIENTIFIC PUBLISHING CO., 2004. http://dx.doi.org/10.1142/9781860945465_0002.

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"Column Dynamics." In Batch Distillation, 63–94. CRC Press, 2011. http://dx.doi.org/10.1201/b11705-10.

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Macháĉek, Jiří, and Josef Kotyk. "MULTIVARIABLE CONTROL OF DISTILLATION COLUMN." In Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes (Dycord'95), 185–90. Elsevier, 1995. http://dx.doi.org/10.1016/b978-0-08-042368-5.50035-6.

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Varga, E. I., G. Z. Kovács, S. B. Jørgensen, and K. M. Hangos. "ROBUST ANALYSIS OF DISTILLATION COLUMN DYNAMICS." In Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes (Dycord'95), 333–38. Elsevier, 1995. http://dx.doi.org/10.1016/b978-0-08-042368-5.50057-5.

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Koggersbøl, A., and S. Bay Jørgensen. "VERIFICATION OF A DISTILLATION COLUMN BENCHMARK." In Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes (Dycord'95), 495–500. Elsevier, 1995. http://dx.doi.org/10.1016/b978-0-08-042368-5.50081-2.

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Koggersbøl, A., and S. Bay Jørgensen. "DISTILLATION COLUMN CONTROL BENCHMARKS: Four Typical Problems." In Dynamics and Control of Chemical Reactors, Distillation Columns and Batch Processes (Dycord'95), 323–25. Elsevier, 1995. http://dx.doi.org/10.1016/b978-0-08-042368-5.50055-1.

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HASEBE, Shinji, Badhrulhisham B. ABDUL AZIZ, Iori HASHIMOTO, and Tetsuya WATANABE. "OPTIMAL DESIGN AND OPERATION OF COMPLEX BATCH DISTILLATION COLUMN." In Interactions Between Process Design and Process Control, 177–82. Elsevier, 1992. http://dx.doi.org/10.1016/b978-0-08-042063-9.50026-1.

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Denes, Ferenc, Peter Lang, and Xavier Joulia. "New generalised double-column system for batch heteroazeotropic distillation." In Computer Aided Chemical Engineering, 366–70. Elsevier, 2011. http://dx.doi.org/10.1016/b978-0-444-53711-9.50074-2.

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Zumoffen, D., L. Garyulo, M. Basualdo, and L. Jiménez. "Predictive functional control applied to multicomponent batch distillation column." In Computer Aided Chemical Engineering, 1465–70. Elsevier, 2005. http://dx.doi.org/10.1016/s1570-7946(05)80086-0.

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Conference papers on the topic "Batch distillation column"

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Maiti, Debadrita, Amiya K. Jana, Amar Nath Samanta, Swapan Paruya, Samarjit Kar, and Suchismita Roy. "Heat Integration in Batch Distillation Column." In INTERNATIONAL CONFERENCE ON MODELING, OPTIMIZATION, AND COMPUTING (ICMOS 20110). AIP, 2010. http://dx.doi.org/10.1063/1.3516310.

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Maulidda, Renny, Pranoto Hidaya Rusmin, Arief Syaichu Rohman, Egi Muhammad Idris Hidayat, and Dimitri Mahayana. "Modeling and Simulation of Mini Batch Distillation Column." In 2017 5th International Conference on Instrumentation, Communications, Information Technology, and Biomedical Engineering (ICICI-BME). IEEE, 2017. http://dx.doi.org/10.1109/icici-bme.2017.8537724.

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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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Ayu, Wirenda Sekar, Pranoto Hidaya Rusmin, and Egi M. I. Hidayat. "Robust PID Control Design in CPS-based Batch Distillation Column." In 2019 6th International Conference on Electrical Engineering, Computer Science and Informatics (EECSI). IEEE, 2019. http://dx.doi.org/10.23919/eecsi48112.2019.8977083.

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Zhiyun Zou, Dehong Yu, Zhen Hu, Ning Guo, Luping Yu, and Wenqiang Feng. "State Space Modeling and Predictive Control of a Binary Batch Distillation Column." In 2006 6th World Congress on Intelligent Control and Automation. IEEE, 2006. http://dx.doi.org/10.1109/wcica.2006.1714285.

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Mardyaningsih, Wedar Panji, Pranoto Hidaya Rusmin, and Budi Rahardjo. "Anomaly Detection and Data Recovery on Mini Batch Distillation Column based Cyber Physical System." In 2019 6th International Conference on Electrical Engineering, Computer Science and Informatics (EECSI). IEEE, 2019. http://dx.doi.org/10.23919/eecsi48112.2019.8977070.

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Harjamulya, Handy, Pranoto Hidaya Rusmin, Egi M. I. Hidavat, and Arief Syaichu-Rohman. "Design and Implementation of MPC for Energy Optimization of Boiler in Batch Distillation Column." In 2019 6th International Conference on Electrical Engineering, Computer Science and Informatics (EECSI). IEEE, 2019. http://dx.doi.org/10.23919/eecsi48112.2019.8977079.

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Dwisaputra, Indra, Pranoto Hidaya R., Arief Syaichu R., Egi M. I. Hidayat, Dimitri Mahayana, and Anton Sapto Handoko. "Fuzzy Logic Controller Design and Implementation for Delayed and Nonlinear Time Variant Batch Distillation Column." In 2017 5th International Conference on Instrumentation, Communications, Information Technology, and Biomedical Engineering (ICICI-BME). IEEE, 2017. http://dx.doi.org/10.1109/icici-bme.2017.8537722.

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Susanti, Novita Dwi, Arief Syaichu Rohman, Pranoto Hidaya Rusmin, and Eko Joni Pristianto. "Design of Ethanol Concentration Measurement System Using Specific Gravity Approach for Batch Distillation Column Automation." In 2019 International Conference on Radar, Antenna, Microwave, Electronics, and Telecommunications (ICRAMET). IEEE, 2019. http://dx.doi.org/10.1109/icramet47453.2019.8980445.

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BAI, PENG, JING FANG, JUNFENG YAO, and MIN SHENG. "DESIGN AND OPERATION OF A BATCH EXTRACTIVE RECTIFICATION COLUMN WITH A BOTTOM EQUILIBRIUM DISTILLATION STILL." In Proceedings of the 4th International Conference. WORLD SCIENTIFIC, 2004. http://dx.doi.org/10.1142/9789812702623_0036.

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You might also be interested in the extended bibliographies on the topic 'Batch distillation column' for particular source types:
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