Relevant bibliographies by topics / CSTR

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  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
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Academic literature on the topic 'CSTR'

Author: Grafiati
Published: 4 June 2021
Last updated: 9 February 2022

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Journal articles on the topic "CSTR"

1

Azizan, Amizon, and Nornizar Anuar. "Simulating Trambouze reaction for a series reactor." Malaysian Journal of Chemical Engineering and Technology (MJCET) 3, no. 1 (November 30, 2020): 1. http://dx.doi.org/10.24191/mjcet.v3i1.10930.

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Simulating the existing data on Trambouze reaction is compiled in this article. The objective of the work is to present the change of volumetric flow rate and the inlet concentration of key reactant A in a series continuous stirred tank reactor-plug flow reactor (CSTR-PFR) configurations. The volumetric flow rate does not affect selectivity and conversion for a constant volumetric flow rate operating condition, entering CSTR and PFR, at a specific concentration of reactant. The CSTR-PFR series reactor configuration is proposed for the aim of maximizing the selectivity of the desired product B in comparison to the undesired products X and Y. CSTR as the first reactor is capable to achieve the maximum conversion at the highest selectivity of A. PFR is then proposed after CSTR in a configuration of CSTR-PFR, to allow higher conversion value to be achieved for the resulted outlet stream conditions coming out of the first reactor, CSTR. Both reactors commonly encounter a decrease in the initial concentration of A and an increase to the formation of other products. The CSTR entering volumetric flow rate influence the volume sizes needed in achieving the maximum selectivity and conversion
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Chang, Kil Sang, Jae Youn Kim, and Hyun-Ku Rhee. "Intricate CSTR dynamics." Korean Journal of Chemical Engineering 6, no. 2 (April 1989): 69–80. http://dx.doi.org/10.1007/bf02697482.

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3

Sudha, T. "Analysis of Proportional Integral Derivative Controller Parameters for CSTR." WSEAS TRANSACTIONS ON SYSTEMS AND CONTROL 16 (July 13, 2021): 387–95. http://dx.doi.org/10.37394/23203.2021.16.34.

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Continuous Stirred Tank Reactor (CSTR) plays a vital role and presents a various scope of researchers in the field of control and chemical engineering which exhibits of highly nonlinear behaviour and has wide operating ranges. Different control methods have been implemented on CSTR to control these parameters. Tragically, in the realcase, the behaviour of the CSTR is very different from that expected ideal CSTR which leads to the outcomes of the wrong product. However, it is a challenging task for every engineer to control the CSTR.PID controller has been proposed for adjust enhanced PID parameters in a CSTR operation utilizing a weighted mix of target capacities. Streamlining of PID controller parameters is the key objective of concoction and biochemical businesses. PID controllers have restricted the working scope of procedures with effective nonlinearity. This work considers some issues in CSTR and presents the efforts of existing researchers and it comes into view as an essential new method to adjust the control parameters. This work plans to investigate the various techniques in CSTR along with its solutions and these schemes have been surveyed in this work. This survey presents the comparison of various methods for optimizing parameters in CSTR are employed and compared with certain parameters.
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Trishch, Vitaliy, Yurii Beznosyk, Gregory Yablonsky, and Denis Constales. "The phenomenon of conservative-perturbed equilibrium in conditions different reactors." Proceedings of the NTUU “Igor Sikorsky KPI”. Series: Chemical engineering, ecology and resource saving, no. 1 (March 30, 2021): 38–46. http://dx.doi.org/10.20535/2617-9741.1.2021.228137.

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Finding the optimal mode is a conceptual problem. The most important indicator that reflects the perfection of a chemical reactor is the intensity of the process in it. The phenomenon of conservatively perturbed-equilibrium (CPE) in the conditions of different types of reactors (in acyclic and cyclic systems) was studied: the ideal displacement reactor ("steady-state plug flow reactor, PFR") and the ideal mixing reactor ("steady-state continuous stirred tank reactor, CSTR"). For the acyclic reaction, the time of extremum onset was less in CSTR by ≈2.1%, but the concentration of substance B in the extremum in PFR was greater by ≈17.2% than in CSTR. For the cyclic reaction, the time of extremum onset was less in CSTR by ≈5.6%, but the concentration of substance B in the extremum in PFR was greater by ≈11.6% than in CSTR. For the acyclic and cyclic reaction in PFR, the time of occurrence of the extremum of the cyclic reaction was lower by ≈44.2% than in the acyclic, but the concentration of substance B in the extremum of the acyclic reaction was greater by ≈24.8% than in the cyclic reaction. For the acyclic and cyclic reaction in CSTR, the time of occurrence of the extremum of the cyclic reaction was lower by ≈46.2% than in the acyclic, but the concentration of substance B in the extremum in the acyclic reaction was greater by ≈18.9% than in the cyclic reaction. The cyclic system showed a shorter time for the onset of the extremum, but the acyclic reaction system showed a higher concentration of substance B at the extremum in PFR and CSTR. Although the time of extremum onset was the lowest in CSTR in the cyclic system, the concentration of substance B in the extremum was highest in the PFR in the acyclic system. Therefore (from our systems and reactors) the acyclic system in PFR shows the best characteristics. The extremum in transient modes is always observed for acyclic and cyclic complex reactions in both reactors, both in PFR and in CSTR. The phenomenon of conservatively perturbed-equilibrium is manifested in both PFR and CSTR. With the same rate constants, the acyclic system in PFR is characterized by higher values of "over equilibrium" conversion than the acyclic system in CSTR. Similarly, with the same rate constants, the cyclic system in PFR is characterized by higher values of "over equilibrium" conversion than the cyclic system in CSTR. The time of extremum onset is less in CSTR. This is true for acyclic and cyclic systems. The greater the difference between the initial concentrations of the two substances, the greater the "over equilibrium" concentration of the third substance, the initial concentration of which was equilibrium. At our values of kinetic parameters, the sensitivity of the time of occurrence of the extremum of the same reaction in different reactors (PFR and CSTR) is small (up to ≈5.6%), and at different reactions (acyclic and cyclic), but in one type of reactor (PFR or CSTR) - significant, reaching ≈46.2%.
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Jia, Xiao Yi, Yu Tian Lin, Hui Bin Lin, Ling Gao, Jian Qun Lin, and Jian Qiang Lin. "Mathematical Modeling of CSTR Bioreactor Control for Production of Recombinant Protein." Advanced Materials Research 894 (February 2014): 311–15. http://dx.doi.org/10.4028/www.scientific.net/amr.894.311.

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Fermentation process using recombinant strain for production of recombinant protein is widely used in commercialization of the biotechnologies. The continuous stirred tank reactor (CSTR) is a typical microbial cultivation method, has the major advantage of high productivity. Mathematical modeling and simulation is useful for analysis and optimization of the CSTR fermentation process. Most of the mathematical models developed for CSTR are black box models without information of the intracellular dynamics and regulations. In this research, a mathematical model is built based on gene regulation for recombinant protein production using CSTR, and simulation is made using this model.
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Caneba, G. T., and Barbara Densch. "Intermittency in nonisothermal CSTR." AIChE Journal 34, no. 2 (February 1988): 333–34. http://dx.doi.org/10.1002/aic.690340219.

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7

Zakaria, Siti Aminah, Mohd Jufri Zakaria, and Mohd Kamaruddin Abd Hamid. "Sustainable Integrated Process Design and Control for a Continuous-Stirred Tank Reactor System." Applied Mechanics and Materials 625 (September 2014): 466–69. http://dx.doi.org/10.4028/www.scientific.net/amm.625.466.

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The objective of this paper is to highlight the use of a two-dimensional (2D) sustainability index in performing a sustainable integrated process design and control (Sustain-IPDC) for a continuous-stirred tank reactor (CSTR) system. Sustain-IPDC for a CSTR system is formulated as a mathematical programming problem and solved by decomposing it into six sequential hierarchical sub-problems: (i) pre-analysis, (ii) design analysis, (iii) controller design analysis, (iv) sustainability analysis, (v) detailed economic analysis, and (vi) final selection and verification. The proposed methodology is applied to the production of cyclohexanone using a CSTR. The results show that the proposed methodology is capable in finding an optimal solution for a CSTR design problem that satisfy design, control, sustainability and economic criteria in an easy and systematic manner.
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Toson, Peter, Pankaj Doshi, and Dalibor Jajcevic. "Explicit Residence Time Distribution of a Generalised Cascade of Continuous Stirred Tank Reactors for a Description of Short Recirculation Time (Bypassing)." Processes 7, no. 9 (September 10, 2019): 615. http://dx.doi.org/10.3390/pr7090615.

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The tanks-in-series model (TIS) is a popular model to describe the residence time distribution (RTD) of non-ideal continuously stirred tank reactors (CSTRs) with limited back-mixing. In this work, the TIS model was generalised to a cascade of n CSTRs with non-integer non-negative n. The resulting model describes non-ideal back-mixing with n > 1. However, the most interesting feature of the n-CSTR model is the ability to describe short recirculation times (bypassing) with n < 1 without the need of complex reactor networks. The n-CSTR model is the only model that connects the three fundamental RTDs occurring in reactor modelling by variation of a single shape parameter n: The unit impulse at n→0, the exponential RTD of an ideal CSTR at n = 1, and the delayed impulse of an ideal plug flow reactor at n→∞. The n-CSTR model can be used as a stand-alone model or as part of a reactor network. The bypassing material fraction for the regime n < 1 was analysed. Finally, a Fourier analysis of the n-CSTR was performed to predict the ability of a unit operation to filter out upstream fluctuations and to model the response to upstream set point changes.
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Delevich, Kristen, Nana J. Okada, Ameet Rahane, Zicheng Zhang, Christopher D. Hall, and Linda Wilbrecht. "Sex and Pubertal Status Influence Dendritic Spine Density on Frontal Corticostriatal Projection Neurons in Mice." Cerebral Cortex 30, no. 6 (February 9, 2020): 3543–57. http://dx.doi.org/10.1093/cercor/bhz325.

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Abstract In humans, nonhuman primates, and rodents, the frontal cortices exhibit grey matter thinning and dendritic spine pruning that extends into adolescence. This maturation is believed to support higher cognition but may also confer psychiatric vulnerability during adolescence. Currently, little is known about how specific cell types in the frontal cortex mature or whether puberty plays a role in the maturation of some cell types but not others. Here, we used mice to characterize the spatial topography and adolescent development of cross-corticostriatal (cSTR) neurons that project through the corpus collosum to the dorsomedial striatum. We found that apical spine density on cSTR neurons in the medial prefrontal cortex decreased significantly between late juvenile (P29) and young adult time points (P60), with females exhibiting higher spine density than males at both ages. Adult males castrated prior to puberty onset had higher spine density compared to sham controls. Adult females ovariectomized before puberty onset showed greater variance in spine density measures on cSTR cells compared to controls, but their mean spine density did not significantly differ from sham controls. Our findings reveal that these cSTR neurons, a subtype of the broader class of intratelencephalic-type neurons, exhibit significant sex differences and suggest that spine pruning on cSTR neurons is regulated by puberty in male mice.
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Yan, J., and Y. Y. Hu. "Comparison of partial nitrification to nitrite for ammonium-rich organic wastewater in sequencing batch reactors and continuous stirred-tank reactor at laboratory-scale." Water Science and Technology 60, no. 11 (December 1, 2009): 2861–68. http://dx.doi.org/10.2166/wst.2009.719.

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The combined partial nitrification/Anammox process is especially suitable for the treatment of influents with low C/N ratio. However, many nitrogenous wastewater are also rich in organics. Two systems (continuous stirred-tank reactor (CSTR) and sequencing batch reactor (SBR)) are commonly used to achieve nitrite accumulation, but no complete comparison between these two systems for treating different wastewater has been reported. The objective of this paper was to compare the partial nitrification in CSTR and SBR for the treatment of ammonium-rich organic wastewater. The result showed that it took a shorter time to startup partial nitrification in CSTR, but SBR was a better option for treating ammonium-rich organic wastewater with C/N lower than 0.34. With increase HRT to 48 h, excellent nitrite accumulation could be achieved in both reactors for wastewater containing landfill leachate. For subsequent anammox, CSTR was more suitable when leachate percentage ranged from 35% to 40%.
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Dissertations / Theses on the topic "CSTR"

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Tanaka, Ken. "Control of solution MMA polymerization in a CSTR." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1997. http://www.collectionscanada.ca/obj/s4/f2/dsk2/ftp04/mq22260.pdf.

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Barbosa, Junior Vandoel Pedro. "Estrategias de controle de operação de reatores CSTR." [s.n.], 1992. http://repositorio.unicamp.br/jspui/handle/REPOSIP/267333.

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Orientador: Rubens Maciel Filho
Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Quimica
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Resumo: : O controle de processos químicos é um fator determinante para o bom desempenho de toda a planta. No entanto, o seu sucesso vai depender do desenvolvimento de estruturas de controle adequadas. Neste trabalho foram propostas e investigadas várias estruturas de controle com o objetivo de obter o controle de reatores químicos ¿off-line¿ e ¿on-line¿. Para tanto foram utilizadas técnicas de controle não convencionais. O sistema considerado é um reator tanque contínuo agitado (CSTR) não isotérmico para reações químicas do tipo A 'seta¿ B ou A 'seta¿ B 'seta¿ C (consideradas exotérmicas, irreversíveis e com cinéticas de primeira ordem), onde pretende-se maximizar o produto B. O estudo deste tipo de sistema tem relevância para muitos processos na indústria química e em processos biotecnológicos. Embora o sistema seja de parâmetros concentrados, o fato de ser multivariável e ter um modelo matemático determinístico não linear, leva-o a ter um comportamento dinâmico complexo. Um estudo dinâmico abrangente do sistema, para perturbações múltiplas nas variáveis de entrada, foi realizado. A metodologia proposta para analisar tais efeitos mostrou-se conveniente na definição de futuras políticas de controle e de operação. Feita a análise dinâmica do sistema iniciou-se os estudos de otimização através de um procedimento visando a definição de ¿set-point¿ para operação ótima do reator, estratégias e implementação de algoritmos de controle... Observação: O resumo, na íntegra, poderá ser visualizado no texto completo da tese digital
Abstract: The control of chemical processes is a determining factor to a good performance of the whole plant. However, its success will be highly restricted to the development of suitable control structures. In this work, it was proposed and investigated several structures of control looking for obtaing suitable off-line and on-line control of chemical reactor. For that some non-conventional techiniques were used. A non-isothermic continuous stirred tank reactor (CSTR) to chemical reactions of the type A 'seta¿ B ou A 'seta¿ B 'seta¿ C (considered exothermic, irreversible with first order kinetics) was used as the system, where the control objective is to maximize product b. the study of this system is of major importance in many process is of the chemical and biotechnological industries. In spite of being a lumped parameter system, the process multivariable and nonlinear so that it has a complex dynamic behaviour. A comprehensive dynamic study for simultaneous perturbations of the inputs was carried out. The proposed methodology to analyse such effects showed out be very convenient in the definitions of control strategies and operational policies. Made the dynamic analyse of the system was began the optimization study through a procedure to define the set-point for the reactor optimum operation, strategies and implementation of control algorithm... Note: The complete abstract is available with the full electronic digital thesis or dissertations
Mestrado
Mestre em Engenharia Química
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Murphy, Terry 1955. "Residence time distribution of solid particles in a CSTR." Thesis, McGill University, 2002. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=79251.

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When mixing in a tank is insufficient solid particles are known to form a concentration gradient along the height. The one-dimensional sedimentation dispersion model provides a relationship between mixing parameters and the solids concentration gradient. An investigation of the relationship between the solid mixing properties and the solids residence time distribution, as derived from the sedimentation dispersion model has been conducted. Experimental results show that the solids residence time distribution was a function of particle size and differed from that for the liquid phase. An empirical correlation for the solids Peclet number to predict the residence time distribution of the particles is proposed. A single parameter model to predict the solids residence time distribution as a function of particle size is presented. The influence of the particle concentration gradient on the mean conversion obtained in the reactor for two different cases is examined.
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Ali, Fathei M. "On the nonlinear chemical dynamics of the imperfectly mixed CSTR." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/ftp03/NQ33891.pdf.

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SANTOS, Tarcísio David KOnna Nunes. "Simulação em CFP de um reator CSTR para produção de biodíesel." Universidade Federal de Campina Grande, 2016. http://dspace.sti.ufcg.edu.br:8080/jspui/handle/riufcg/301.

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Este trabalho propôs um modelo matemático para um reator do tipo CSTR (continuous stirred-tank reactor) partindo de dados experimentais da cinética da reação de transesterificação entre o óleo de soja e o acetato de metila, tendo como catalisador uma enzima, a Candida Antartica. Um volume foi proposto para reator para que o tempo médio de residência da mistura reacional fosse suficiente tal que o rendimento esperado, com base nos dados obtidos pelo Matlab®, fosse obtido na saída do reator. O estudo reacional fluidodinâmico foi feito utilizando o software comercial ANSYS® versão 15.0. Duas configurações do reator foram propostas otimização, afim de tornar o processo o mais homogêneo possível, tentando atingir as configurações do reator de mistura perfeita. Os impelidores utilizados foram o tipo pás retas inclinadas e o ripo Ribbon (Âncora), afim de avaliar qual dos impelidores consegue o rendimento satisfatório com menor potência de operação. A potência requerida foi determinada através das equações para misturadores mecânicos, sendo avaliado apenas como variável a rotação das pás.
This work proposes a mathematical model to a reactor of CSTR-type (Continuous Stirred-tank reactor) starting from experimental data of the kinetics of transesterification of soybean oil and methyl acetate, with the catalyst enzyme, Candida Antarctica. A reactor volume was proposed for the average residence time of the reaction mixture was sufficient such that the expected yield, based on data obtained by Matlab, was obtained in the reactor outlet. The reaction fluid dynamic study was done using the commercial software ANSYS® version 15.0. The optimization of the reactor was proposed by comparing the reactor operation with two impellers separately in order to make the process more homogeneous as possible, trying to achieve the perfect blend of reactor configurations. The impellers used were the type inclined straight blades and Ribbon RIPO (Anchor), to determine which of the impellers can the satisfactory performance with lower power operation. The required power was determined by the equations for mechanical mixers, being rated only as a variable rotation of the blades
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SOARES, Arianne de Freitas Barros. "Análise e avaliação entrópica de reações múltiplas consecutivas em reator CSTR." Universidade Federal de Campina Grande, 2017. http://dspace.sti.ufcg.edu.br:8080/jspui/handle/riufcg/2022.

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O presente trabalho estende a metodologia de análise e otimização de processos químicos via minimização da taxa de produção de entropia a um sistema considerado complexo e pouco explorado pela metodologia adotada. Com o intuito de determinar as condições ótimas operacionais do processo, um sistema de reações múltiplas, genéricas e consecutivas conduzidas em um reator de mistura perfeita foi analisado. Tendo em vista que o produto intermediário é o de interesse comercial, o desenvolvimento da metodologia foi baseado nos balanços de massa e energia associados ao balanço entrópico objetivando a minimização da taxa de produção de entropia da reação de interesse. Em conformidade com estudos antecedentes, o procedimento de otimização revelou que a obtenção de uma relação entre a temperatura de alimentação e a temperatura de operação é fundamental para que a condição de mínima produção de entropia seja alcançada. Se tratando da temperatura de reação, uma única condição operacional foi considerada ótima do ponto de vista da mínima produção de entropia, maximizando o rendimento do produto desejado; enquanto que a metodologia clássica de análise e otimização sugeriu diversos pontos operacionais, incluindo um que direciona o sistema para a maximização do produto indesejado em detrimento do produto de interesse. Por se tratar de reações consecutivas, um parâmetro construtivo do reator também foi analisado para alcançar a condição de mínima entropia. A otimização entrópica do tempo de residência revelou que quanto maior for seu valor menor será a taxa de produção de entropia. Uma análise econômica de modo simplificado foi aplicada ao sistema com o intuito de se configurar um critério de seleção de tal parâmetro. Os resultados obtidos revelaram uma nova condição operacional capaz de reduzir os custos energéticos do processo e melhorar o desempenho reacional do sistema.
The present study extends the methodology of analysis and optimization of chemical process by minimizing the entropy rate production to a system considered complex and still not explored by the adopted methodology. In order to determinate the optimal operational conditions of the process, a system of multiple generic and consecutive reactions conducted in a perfect mixing reactor was analyzed. Since the intermediate product is of commercial interest, the development of the methodology was based on the mass and energy balances associated with the entropic balance aiming to minimize the entropy rate production of the reaction of interest. In accordance with previous studies, the optimization procedure revealed that obtaining a relation between inlet and operating temperatures is essential to reach the minimum entropy production condition. If treating of reaction temperature, a single operational condition was considered optimal from the point of view of minimum entropy production, while the classical analysis methodology suggested several operating points. Because it is a consecutive reaction, a constructive parameter of the reactor was also analyzed to reach the minimum entropy condition. The entropic optimization of the residence time revealed that the higher its value the lower is the entropy rate production. A simplified economic analysis was applied in order to configure a selection criterion for such parameter. The results reveals a new operating condition capable of reducing the energy costs of the process and improving the reactive performance of the system.
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Mendiburu, Díaz Henry A. "Diseño de un neurocontrolador dinámico (DBP) aplicado a un reactor químico continuo (CSTR)." Master's thesis, Pontificia Universidad Católica del Perú, 2005. http://tesis.pucp.edu.pe/repositorio/handle/123456789/138.

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La presente tesis se compone de cuatro capítulos: en el primer capítulo se plantea los objetivos de la esta investigación y se realiza una recopilación de información referente a investigaciones relacionadas con el control y la automatización de reactores químicos CSTR. En el segundo capítulo realiza una introducción teórica sobre el reactor tanque agitado continuo, así mismo se desarrolla el modelo matemático de un reactor químico de este tipo, el cual servirá para la simulación del sistema a controlar. En el tercer capítulo se lleva a cabo el desarrollo de los criterios de diseño y parámetros de sintonización de los diversos controladores implementados para aplicarlos al reactor. En el cuarto capítulo se presentan las simulaciones del sistema sometido a la acción de control de los diversos controladores, para luego elaborar un análisis de la performance de cada uno, y finalmente establecer la superioridad del neurocontrolador dinámico frente a otros controladores.
Tesis
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Basu, Nandini. "Nonlinear chemical phenomena in a continuously stirred tank reactor (CSTR) containing chlorine dioxide and sulfite /." free to MU campus, to others for purchase, 2004. http://wwwlib.umi.com/cr/mo/fullcit?p1426045.

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Temeng, Kwaku Ofosu. "The design and evaluation of a control scheme for emulsion polymerization in a tube-CSTR system." Diss., Georgia Institute of Technology, 1987. http://hdl.handle.net/1853/10019.

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10

Wolf, Aurel. "Darstellung von Styrol-Glycidylmethacrylat-Copolymeren mit niedrigen Molmassen durch radikalische Polymerisation im CSTR bei hohen Temperaturen." [S.l.] : [s.n.], 2000. http://deposit.ddb.de/cgi-bin/dokserv?idn=962822604.

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Books on the topic "CSTR"

1

Tyagi, Rajesh. Control of pH in a continuous stirred tank reactor (CSTR). Ottawa: National Library of Canada = Bibliothèque nationale du Canada, 1993.

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Edwards, J. B. Use of the Riccati equation on-line for adaptively controlling a CSTR chemical reactor. Sheffield: University of Sheffield, Dept. of Automatic Control and Systems Engineering, 1995.

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OAU/STRC, Inter-African Symposium on New Renewable and Solar Energies (3rd 1997 Pretoria South Africa). Third OAU/STRC Inter₋African Symposium on New, Renewable and Solar Energies: Troisieme Symposium Inter₋African OAU/CSTR sur les energies nouvelles, renouvelables et solaires. Pretoria: Dept. of Minerals and Energy, 1999.

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(Ghana), Council for Scientific and Industrial Research. CSIR handbook. Accra, Ghana: CSIR Secretariat, 1999.

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Reisinger, Attila. Cser sógor. Budapest: Littera Nova, 2010.

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(India), Council of Scientific &. Industrial Research. CSIR profile 2005. New Delhi: Council of Scientific & Industrial Research, 2005.

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Council of Scientific & Industrial Research (India). CSIR directory, 2006. New Delhi: Council of Scientific & Industrial Research, 2006.

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Mian, Yawar Hanif. CSR Pakistan. Lahore: Yawar Hanif Mian, 2009.

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Mian, Yawar Hanif. CSR Pakistan. Lahore: Yawar Hanif Mian, 2009.

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Urip, Sri, ed. CSR Strategies. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2012. http://dx.doi.org/10.1002/9781119199595.

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Book chapters on the topic "CSTR"

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Martinez-Guerra, Rafael, and Juan Luis Mata-Machuca. "Fault Detection in CSTR Using Nonlinear Observers." In Understanding Complex Systems, 21–32. Cham: Springer International Publishing, 2013. http://dx.doi.org/10.1007/978-3-319-03047-0_2.

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Manimozhi, M., and R. Meenakshi. "Multiloop IMC-Based PID Controller for CSTR Process." In Proceedings of the International Conference on Soft Computing Systems, 615–25. New Delhi: Springer India, 2015. http://dx.doi.org/10.1007/978-81-322-2671-0_59.

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Kroiss, Helmut, and Karl Svardal. "CSTR Reactors and Contact Processes in Industrial Wastewater Treatment." In Biotechnology, 479–91. Weinheim, Germany: Wiley-VCH Verlag GmbH, 2008. http://dx.doi.org/10.1002/9783527620944.ch23.

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Ranjan, Ankita, and Sarbani Chakraborty. "Phase Portrait Analysis of Continuous Stirred Tank Reactor (CSTR)." In Nanoelectronics, Circuits and Communication Systems, 177–92. Singapore: Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-15-7486-3_18.

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Taylor, T. W., and W. Geiseler. "Periodic Perturbation of Limit Cycles in an Isothermal CSTR." In Temporal Order, 122–25. Berlin, Heidelberg: Springer Berlin Heidelberg, 1985. http://dx.doi.org/10.1007/978-3-642-70332-4_17.

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Bar-Eli, K. "Oscillations in a CSTR Affected by the Pump Periodicity." In Temporal Order, 126–27. Berlin, Heidelberg: Springer Berlin Heidelberg, 1985. http://dx.doi.org/10.1007/978-3-642-70332-4_18.

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Vojtesek, Jiri, and Petr Dostál. "Control of Concentration inside CSTR Using Nonlinear Adaptive Controller." In Nostradamus 2014: Prediction, Modeling and Analysis of Complex Systems, 195–204. Cham: Springer International Publishing, 2014. http://dx.doi.org/10.1007/978-3-319-07401-6_19.

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Murugan, B., R. Vinodha, and B. Shoba. "Fuzzy Cluster based PID Controller for a CSTR Process." In Lecture Notes in Electrical Engineering, 283–93. Singapore: Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-16-0336-5_23.

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Schnürer, A., I. Bohn, and J. Moestedt. "Protocol for Start-Up and Operation of CSTR Biogas Processes." In Springer Protocols Handbooks, 171–200. Berlin, Heidelberg: Springer Berlin Heidelberg, 2016. http://dx.doi.org/10.1007/8623_2016_214.

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Mukherjee, Deep, Palash Kundu, and Apurba Ghosh. "Analysis of Conventional and Fractional-Order Controllers for Nonlinear CSTR System." In Lecture Notes in Electrical Engineering, 167–74. Singapore: Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-15-7511-2_15.

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Conference papers on the topic "CSTR"

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Utkin, Victor A., and Svetlana I. Gulyukina. "Block approach for CSTR Control." In 2020 International Russian Automation Conference (RusAutoCon). IEEE, 2020. http://dx.doi.org/10.1109/rusautocon49822.2020.9208071.

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Hazerchi, Mohamed, and Rachid Illoul. "Tracking PDC controller for CSTR." In 2015 3rd International Conference on Control, Engineering & Information Technology (CEIT). IEEE, 2015. http://dx.doi.org/10.1109/ceit.2015.7233084.

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Wang, Zaiying, Ye Zhang, and Dong Li. "Temperature Optimization Control of CSTR." In 2020 IEEE International Conference on Information Technology,Big Data and Artificial Intelligence (ICIBA). IEEE, 2020. http://dx.doi.org/10.1109/iciba50161.2020.9276793.

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Sabura Banu, U., and G. Uma. "Modelling of CSTR by fuzzy clustering." In 2006 India International Conference on Power Electronics (IICPE 2006). IEEE, 2006. http://dx.doi.org/10.1109/iicpe.2006.4685400.

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Varshney, Tarun, Ruchi Varshney, and Satya Sheel. "ANN based IMC scheme for CSTR." In the International Conference. New York, New York, USA: ACM Press, 2009. http://dx.doi.org/10.1145/1523103.1523211.

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Almalki Al-Jehani, Nejoud, Hazem N. Nounou, and Mohamed N. Nounou. "Fuzzy control of a CSTR process." In 2012 8th International Symposium on Mechatronics and its Applications (ISMA). IEEE, 2012. http://dx.doi.org/10.1109/isma.2012.6215176.

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Hoang, H., F. Couenne, Y. Le Gorrec, and D. Dochain. "Thermodynamics based stabilitization of CSTR networks." In 2012 IEEE 51st Annual Conference on Decision and Control (CDC). IEEE, 2012. http://dx.doi.org/10.1109/cdc.2012.6427055.

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Wright, Raymond A., and Costas Kravaris. "Nonlinear pH Control in a CSTR." In 1989 American Control Conference. IEEE, 1989. http://dx.doi.org/10.23919/acc.1989.4790431.

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Cinar, A., K. Rigopoulos, S. M. Meerkov, and X. Shu. "Nonlinear Control of an Exothermic CSTR." In 1986 American Control Conference. IEEE, 1986. http://dx.doi.org/10.23919/acc.1986.4789083.

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Cinar, A., K. Rigopoulos, S. M. Meerkov, and X. Shu. "Vibrational Control of an Exothermic CSTR." In 1986 American Control Conference. IEEE, 1986. http://dx.doi.org/10.23919/acc.1986.4789145.

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Reports on the topic "CSTR"

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Lee, D. D. Test Results for CSTR Test 4. Office of Scientific and Technical Information (OSTI), May 2001. http://dx.doi.org/10.2172/786329.

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Lee, D. D. Test Results for CSTR Test 3. Office of Scientific and Technical Information (OSTI), October 2000. http://dx.doi.org/10.2172/814058.

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Liu, D. D. S., and D. J. Patmore. Comparison of pitch conversions from experiments using CSTR and tubular reactors in the CANMET hydrocracking process. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1985. http://dx.doi.org/10.4095/302572.

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Liu, D. D. S., D. J. Patmore, J. S. H. Tscheng, and A. K. Jain. Upgrading of heavy oil and residuum by the CANMET hydrocracking process: comparison of pitch conversion from experiments using CSTR and tubular reactors. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1985. http://dx.doi.org/10.4095/302591.

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Baich, M. A. CST/FRIT Settling, CST Particle Size Reduction and CST Loading. Office of Scientific and Technical Information (OSTI), August 2000. http://dx.doi.org/10.2172/761150.

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Rockward, Tommy, Christopher Jesse Romero, Eric Lanich Brosha, and Rangachary Mukundan. CSTT Update: Fuel Quality Analyzer. Office of Scientific and Technical Information (OSTI), January 2019. http://dx.doi.org/10.2172/1492560.

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Brosha, Eric L., Roger W. Lujan, Rangachary Mukundan, Tommy Rockward, Christopher J. Romero, Stefan Williams, and Mahlon S. Wilson. CSTT Update: Fuel Quality Analyzer. Office of Scientific and Technical Information (OSTI), February 2018. http://dx.doi.org/10.2172/1419742.

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Pina, Cesar A. ARPA/CSTO Rapid VLSI Implementation. Fort Belvoir, VA: Defense Technical Information Center, July 1993. http://dx.doi.org/10.21236/ada269170.

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Wittekind, W. D. ,. Westinghouse Hanford. CSER 96-023: CSER for PFP glovebox HC-21A with 4.4 kilogram plutonium cans. Office of Scientific and Technical Information (OSTI), December 1996. http://dx.doi.org/10.2172/301345.

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Pang, Xiaoying. CSR for drift. Office of Scientific and Technical Information (OSTI), August 2014. http://dx.doi.org/10.2172/1159042.

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