Relevant bibliographies by topics / Semi-batch reactor

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Academic literature on the topic 'Semi-batch reactor'

Author: Grafiati
Published: 4 June 2021
Last updated: 2 February 2022

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Dissertations / Theses on the topic "Semi-batch reactor"

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Pirgalioglu, Saltuk. "Catalytic Ozonation Of Dye Solutions In A Semi-batch Reactor." Master's thesis, METU, 2008. http://etd.lib.metu.edu.tr/upload/3/12610158/index.pdf.

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Treatment of textile wastewaters containing dye materials using the conventional methods based on biological treatment is not possible. In order to overcome this problem, ozonation based on the oxidation of organic pollutants with ozone gas dissolved in aqueous phase have been studied widely. Catalytic ozonation and advanced oxidation processes (AOP) are also used in order to increase the efficiency of sole ozonation In this work, catalytic ozonation processes in the presence of Copper Sulfide (CuS) powder and a synthesized catalyst by the impregnation of iron on alumina (Fe/Al2O3) were studi
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Agarwal, Naveen. "Nonlinear model predictive control of a semi-batch emulsion polymerization reactor." Thesis, Georgia Institute of Technology, 1993. http://hdl.handle.net/1853/8456.

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Calzado, Palomino Luis Enrique. ""Nickel precipitation by ozone oxidation in a semi-batch bubble reactor." Thesis, McGill University, 2003. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=19537.

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The research aims to develop the use of ozone in nickel oxidation-precipitation from dilute solutions. The process presents three main steps: ozone transfer from gas to liquid, ozone decomposition by hydroxyl ions, and nickel oxidation-precipitation. Each step was studied using a semi-batch bubble reactor. For ozone gas-liquid transfer, a methodology to calculate the volumetric mass transfer coefficient ("kLa") was developed. Parameters evaluated included: diffuser porosity, volume of liquid and superficial gas velocity. To calculate the mass transfer coefficient ("kL") interfacial area ("a")
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Contreras, Canteros Francisco Eduardo. "Estudio de la pirólisis catalítica de polietileno en un reactor semi-batch." Tesis, Universidad de Chile, 2014. http://www.repositorio.uchile.cl/handle/2250/116264.

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Magíster en Ciencias de la Ingeniería, Mención Química<br>La creciente producción mundial de plásticos ha generado globalmente un serio problema de acumulación de desechos de origen polimérico, los cuales son mayoritariamente poliolefinas, como el polietileno. Para enfrentar este problema se han estudiado distintas vías de reciclaje, siendo el reciclaje químico uno de los caminos a seguir más estudiado pues permite transformar el desecho plástico en un nuevo compuesto o materia prima (como combustibles o monómeros). De las diversas formas de reciclaje químico la pirólisis catalítica exhibe las
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Ibrahim, W. H. B. W. "Dynamic Modelling and Optimization of Polymerization Processes in Batch and Semi-batch Reactors. Dynamic Modelling and Optimization of Bulk Polymerization of Styrene, Solution Polymerization of MMA and Emulsion Copolymerization of Styrene and MMA in Batch and Semi-batch Reactors using Control Vector Parameterization Techniques." Thesis, University of Bradford, 2011. http://hdl.handle.net/10454/5392.

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Dynamic modelling and optimization of three different processes namely (a) bulk polymerization of styrene, (b) solution polymerization of methyl methacrylate (MMA) and (c) emulsion copolymerization of Styrene and MMA in batch and semi-batch reactors are the focus of this work. In this work, models are presented as sets of differential-algebraic equations describing the process. Different optimization problems such as (a) maximum conversion (Xn), (b) maximum number average molecular weight (Mn) and (c) minimum time to achieve the desired polymer molecular properties (defined as pre-specified va
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Torbacke, Marika. "On the Influence of Mixing and Scaling-Up in Semi-Batch Reaction Crystallization." Doctoral thesis, Stockholm : Tekniska högsk, 2001. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-3197.

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7

Marinangelo, Giovane. "Estudo da copolimerização em emulsão de estireno e acrilato de butila com alto teor de sólidos em reator semicontínuo." Universidade de São Paulo, 2005. http://www.teses.usp.br/teses/disponiveis/3/3137/tde-24102005-151847/.

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Neste trabalho estudou-se o processo de coplimerização em emulsão de estireno e acrilato de butila em processo semicontínuo onde o produto final é um látice com alto teor de sólidos. Foi realizada uma série de experimentos de copolimerização em emulsão em um reator de vidro, empregando receitas com teores de sólidos na faixa de 50 a 64% em massa. Foram estudados os seguintes fatores: teor de sólidos, teor de ácido acrílico, teor de emulsificantes e tempo de adição dos monômeros. Os efeitos estudados são avaliados principalmente em termos de conversão, diâmetro médio das partículas, concentraçã
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Steyer, Christiane Verfasser], Kai [Akademischer Betreuer] [Sundmacher, Jürgen [Akademischer Betreuer] Tomas, and Michael [Akademischer Betreuer] Mangold. "Precipitation of barium sulfate in a semi-batch stirred tank reactor : influence of feeding policy on particle size and morphology / Christiane Steyer. Betreuer: Kai Sundmacher ; Jürgen Tomas ; Michael Mangold." Magdeburg : Universitätsbibliothek, 2012. http://d-nb.info/105391430X/34.

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9

Mendez, Ecoscia Ana Carolina. "Experimental Study of Emulsion Polymerization of Vinylidene Fluoride." Thesis, Lyon, 2016. http://www.theses.fr/2016LYSE1203.

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Le développement d’un procédé de polymérisation en émulsion est complexe de par la nature hétérogène de ce type de réaction. En outre, dans le cas de la polymérisation en émulsion du fluorure de vinylidène, la difficulté est d’autant plus accrue que le monomère est habituellement en phase gazeuse ou supercritique dans les conditions d’intérêt. Or la littérature manque d’informations concernant ce type de procédé de synthèse du PVDF sous une pression comprise entre 30 bar et 90 bar.Ainsi cette thèse a pour objectif de contribuer à une meilleure compréhension des mécanismes cinétiques et de stab
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Derdar, Mawaheb M. Zarok. "Experimental and kinetic modelling of multicomponent gas/liquid ozone reactions in aqueous phase. Experimental investigation and Matlab modelling of the ozone mass transfer and multicomponent chemical reactions in a well agitatated semi-batch gas/liquid reactor." Thesis, University of Bradford, 2010. http://hdl.handle.net/10454/4872.

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Due to the ever increasing concerns about pollutants and contaminants found in water, new treatment technologies have been developed. Ozonation is one of such technologies. It has been widely applied in the treatment of pollutants in water and wastewater treatment processes. Ozone has many applications such as oxidation of organic components, mineral matter, inactivation of viruses, cysts, bacteria, removal of trace pollutants like pesticides and solvents, and removal of tastes and odours. Ozone is the strongest conventional oxidant that can result in complete mineralisation of the organic pol
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