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Relevant bibliographies by topics / Tubular polymerization reactor / Dissertations / Theses

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Dissertations / Theses on the topic 'Tubular polymerization reactor'

Author: Grafiati

Published: 4 June 2021

Last updated: 15 February 2022

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1

Tupe, Ravindra Radhakisan. "Tubular reactor for liquid-phase propylene polymerization." Enschede : University of Twente [Host], 2006. http://doc.utwente.nl/56177.

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2

Banu, Ionut. "Modeling and optimization of tubular polymerization reactors." Phd thesis, Université Claude Bernard - Lyon I, 2009. http://tel.archives-ouvertes.fr/tel-00719401.

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The aim of this thesis is the investigation of modeling and optimization particularities of tubular polymerization reactors. The original work is divided in two sections, the first treating a modeling and optimization study of tubular reactors for methyl methacrylate polymerization in solution, and the second, an experimental and theoretical study of L-lactide reactive extrusion. In the first section, reactor simulations in similar operating conditions were performed in order to select a representative kinetic model among the published kinetic models for MMA solution polymerization. Two widely

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3

Ouzineb, Keltoum. "Emulsion and miniemulsion polymerization : stabilization, tubular reactor and practical applications." Lyon 1, 2003. http://www.theses.fr/2003LYO10022.

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L'objectif de cette thèse est de proposer des applications innovantes pour la polymérisation en émulsion et en mini-émulsion dans différents procédés : réacteur fermé parfaitement agité, semi-continu et continu. Des résultats similaires au réacteur fermé furent obtenus dans le réacteur tubulaire continu pour des taux de solides inférieurs à 30 % en poids. La polymérisation en mini-émulsion s'est alors révélée comme un candidat prometteur en vue d'éliminer les problèmes de démixtion rencontrés à des taux de solide plus important. Dans une étude préliminaire en réacteur fermé nous avons mis en é

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4

Carvalho, Antônio Carlos Sallarés de Mattos. "Desenvolvimento de processo contínuo de copolimerização em emulsão em reator tubular." Universidade de São Paulo, 2008. http://www.teses.usp.br/teses/disponiveis/3/3137/tde-02062008-135006/.

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Os processos industriais de polimerização em emulsão são normalmente realizados em reatores batelada ou semi batelada ou em tanques agitados contínuos (CSTR). Os reatores contínuos têm a vantagem de terem menor porte e de propiciarem melhor controle de qualidade do produto através da redução de variações de batelada a batelada. Além disso, as oscilações periódicas autosustentadas na conversão de monômero e no tamanho da partícula, que são normalmente observadas em reatores do tipo CSTR, podem ser minimizadas em reatores tubulares mediante o uso de dispositivos de mistura estáticos adequados co

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5

Russum, James. "Controlled Radical Polymerizations in Miniemulsions: Advances in the Use of RAFT." Diss., Available online, Georgia Institute of Technology, 2005, 2005. http://etd.gatech.edu/theses/available/etd-10112005-105314/.

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Thesis (Ph. D.)--Chemical and Biomolecular Engineering, Georgia Institute of Technology, 2006.<br>Jones, Christopher, Committee Chair ; Schork, F. Joseph, Committee Co-Chair ; Weck, Marcus, Committee Member ; Meredith, Carson, Committee Member ; Agrawal, Pradeep, Committee Member.

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6

Lucca, Eneida Aparecida de. "Modelagem e simulação de reatores industriais em fase liquida do tipo Loop para polimerização de propileno." [s.n.], 2007. http://repositorio.unicamp.br/jspui/handle/REPOSIP/266238.

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Orientadores: Rubens Maciel Filho, Jose Carlos Costa da Silva Pinto, Priamo Albuquerque Melo Junior<br>Dissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Química<br>Made available in DSpace on 2018-08-10T00:03:32Z (GMT). No. of bitstreams: 1 Lucca_EneidaAparecidade_M.pdf: 1657459 bytes, checksum: 56b6b6c35a2802734e03ed28ceb76c67 (MD5) Previous issue date: 2007<br>Resumo: Reatores tubulares do tipo loop são amplamente empregados nas indústrias de poliolefinas. No caso da produção de polipropileno, compõem a tecnologia Spheripol. São constituídos de duas seções

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7

Nakama, Caroline Satye Martins. "Modelagem estocástica da dispersão axial: aplicação em um reator tubular de polimerização." Universidade de São Paulo, 2016. http://www.teses.usp.br/teses/disponiveis/3/3137/tde-30062016-082711/.

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Reatores tubulares de polimerização podem apresentar um perfil de velocidade bastante distorcido. Partindo desta observação, um modelo estocástico baseado no modelo de dispersão axial foi proposto para a representação matemática da fluidodinâmica de um reator tubular para produção de poliestireno. A equação diferencial foi obtida inserindo a aleatoriedade no parâmetro de dispersão, resultando na adição de um termo estocástico ao modelo capaz de simular as oscilações observadas experimentalmente. A equação diferencial estocástica foi discretizada e resolvida pelo método Euler-Maruyama de forma

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8

Mohammad, Reza Hashemi [Verfasser]. "Optimizing Control and Process Monitoring of a Continuous Polymerization Process in Tubular Reactors / Hashemi Mohammad Reza." Düren : Shaker, 2019. http://d-nb.info/1198600896/34.

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9

Mendoza, Marin Florentino Lazaro. "Modelagem, simulação e analise de desempenho de reatores tubulares de polimerização com deflectores angulares internos." [s.n.], 2004. http://repositorio.unicamp.br/jspui/handle/REPOSIP/267665.

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Orientadores: Rubens Maciel Filho, Liliane Maria Ferrareso Lona<br>Tese (doutorado) - Universidade Estadual de Campinas, Faculdade de Engenharia Quimica<br>Made available in DSpace on 2018-08-04T02:31:19Z (GMT). No. of bitstreams: 1 MendozaMarin_FlorentinoLazaro_D.pdf: 8929110 bytes, checksum: 9041b9e7f02f9a324fa10cde9a962f54 (MD5) Previous issue date: 2004<br>Resumo: O modelo determinístico e processo homopolimerização na emulsão do estireno são aplicados em reator tubular contínuo sem e com deflectores angulares internos sob condição isotérmica e não isotérmica. Os resultados de modelagem

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10

ENRIGHT, THOMAS E. "LIVING/CONTROLLED RADICAL POLYMERIZATION IN A CONTINUOUS TUBULAR REACTOR." Thesis, 2010. http://hdl.handle.net/1974/6246.

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Significant advances have been made in the understanding of living/controlled radical polymerization processes since their discovery in the early 1990’s. These processes enable an unprecedented degree of control over polymer architecture that was previously not possible using conventional radical polymerization processes, and this has made possible the synthesis of many new and interesting materials. However, there has been only limited success in commercializing these new methods. Recently there has been increased focus on the development of more industrially viable processes. Dispersed aq

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11

LI, DE-YUAN, and 李得元. "Study for emulsion polymerization of styrene in a continuous loop tubular reactor." Thesis, 1989. http://ndltd.ncl.edu.tw/handle/05584858015461105289.

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12

林祉成. "Study for emulsion polymerization of vinyl acetate in a continuous loop tubular reactor." Thesis, 1990. http://ndltd.ncl.edu.tw/handle/57142671135357648820.

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13

Paquet, Donald Albert. "Tubular reactors for emulsion polymerization." 1993. http://catalog.hathitrust.org/api/volumes/oclc/29173396.html.

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Thesis (Ph. D.)--University of Wisconsin--Madison, 1993.<br>Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 231-240).

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14

Hipp, Alexander K. "Condensation polymerization in tubular reactors." 1995. http://catalog.hathitrust.org/api/volumes/oclc/33113315.html.

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15

Stevens, Carl John. "Mathematical modeling of bulk and solution free radical polymerization in tubular reactors." 1988. http://catalog.hathitrust.org/api/volumes/oclc/18583841.html.

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