Comportamento da filtração de gases em meios filtrantes de celulose.

Detalhes bibliográficos
Autor(a) principal: Osório, Vanessa Moreira
Data de Publicação: 2006
Tipo de documento: Dissertação
Idioma: por
Título da fonte: Repositório Institucional da UFSCAR
Texto Completo: https://repositorio.ufscar.br/handle/ufscar/3977
Resumo: The present work aims to evaluate, through filtration process and cake detachment, the behavior of two cellulose fiber filtering media with different air permeability values. The powder material used was phosphatic concentrated rock of density 2,99 g/cm3 and its average volumetric diameter of 8,34 µm. The equipment used was constituted of a circular filter, powder feeder which controlled the massic flow and humidity by a microcomputer and a system for control and acquisition of data. The filtering media used were cellulose fibers, Rad More and Rad Plus, supplied by Alhstrom Louveira. The work was accomplished by a successive sequence of filtration and cleaning during 100 filtration cycles using cellulose filtering media. The technique employed for cake removal was reverse air flow. In the experimental procedure, filtration velocity of 10 cm/s was used for maximum pressure drop of 200 mmH2O, and 5 cm/s for maximum pressure drop of 100 mmH2O. Two cleaning velocity were employed for cake removal, 18 and 13 cm/s. The results showed that the filtering media Rad Plus, when submitted to filtration velocity of 10 cm/s and cleaning velocity of 18 cm/s, obtained the best operational condition, as it presented lower values of residual pressure drop for a larger mass retained during the 100 filtration cycles. For different filtration velocity, 10 and 5 cm/s, the filtering media Rad Plus, more porous and more permeable, the amount of particle mass removed was larger than for the filtering media Rad Plus applying cleaning velocity of 18cm/s as the removal force for this cleaning velocity could remove the particles retained in the fibers. For filtration velocity of 5 cm/s, a lower cleaning velocity, 13 cm/s, was enough to remove larger amount of particles, when compared with the filtering media Rad Plus in the same experimental conditions.
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spelling Osório, Vanessa MoreiraAguiar, Mônica Lopeshttp://lattes.cnpq.br/0431688649128529http://lattes.cnpq.br/32827233040572443a2fb3fd-e3c4-43ff-b195-c70800bd46452016-06-02T19:56:28Z2007-10-192016-06-02T19:56:28Z2006-09-15OSÓRIO, Vanessa Moreira. Comportamento da filtração de gases em meios filtrantes de celulose.. 2006. 133 f. Dissertação (Mestrado em Ciências Exatas e da Terra) - Universidade Federal de São Carlos, São Carlos, 2006.https://repositorio.ufscar.br/handle/ufscar/3977The present work aims to evaluate, through filtration process and cake detachment, the behavior of two cellulose fiber filtering media with different air permeability values. The powder material used was phosphatic concentrated rock of density 2,99 g/cm3 and its average volumetric diameter of 8,34 µm. The equipment used was constituted of a circular filter, powder feeder which controlled the massic flow and humidity by a microcomputer and a system for control and acquisition of data. The filtering media used were cellulose fibers, Rad More and Rad Plus, supplied by Alhstrom Louveira. The work was accomplished by a successive sequence of filtration and cleaning during 100 filtration cycles using cellulose filtering media. The technique employed for cake removal was reverse air flow. In the experimental procedure, filtration velocity of 10 cm/s was used for maximum pressure drop of 200 mmH2O, and 5 cm/s for maximum pressure drop of 100 mmH2O. Two cleaning velocity were employed for cake removal, 18 and 13 cm/s. The results showed that the filtering media Rad Plus, when submitted to filtration velocity of 10 cm/s and cleaning velocity of 18 cm/s, obtained the best operational condition, as it presented lower values of residual pressure drop for a larger mass retained during the 100 filtration cycles. For different filtration velocity, 10 and 5 cm/s, the filtering media Rad Plus, more porous and more permeable, the amount of particle mass removed was larger than for the filtering media Rad Plus applying cleaning velocity of 18cm/s as the removal force for this cleaning velocity could remove the particles retained in the fibers. For filtration velocity of 5 cm/s, a lower cleaning velocity, 13 cm/s, was enough to remove larger amount of particles, when compared with the filtering media Rad Plus in the same experimental conditions.O objetivo deste trabalho é avaliar, através do processo de filtração e de remoção das tortas, o comportamento de dois meios filtrantes de fibras de celulose de diferentes permeabilidades. O material particulado utilizado foi o concentrado fosfático de densidade 2,99 g/cm3 e diâmetro médio de partícula de 8,34 µm. O equipamento utilizado era constituído de um filtro circular, alimentador de pó com a vazão mássica e umidade controlada, um microcomputador e um sistema para controle e aquisição de dados. Os meios filtrantes utilizados foram de fibras de celulose, Rad Mais e Rad Plus, fornecidos pela Empresa Alhstrom Louveira. O trabalho foi realizado por uma seqüência sucessiva de filtração e de limpeza durante 100 ciclos de filtração, em meios filtrantes de celulose, sendo que o método de limpeza utilizado, para a remoção das tortas, foi o fluxo de ar reverso. No procedimento experimental de filtração foram utilizadas velocidades de filtração de 10 cm/s, para queda de pressão máxima de 200 mmH2O, e de 5 cm/s, para queda de pressão de 100 mmH2O. Para a remoção das tortas foram utilizadas duas velocidades de limpeza, de 18 cm/s e 13 cm/s. Os resultados mostraram que o meio filtrante Rad Mais, quando submetido à velocidade de filtração de 10 cm/s e velocidade de limpeza de 18 cm/s, obteve a melhor condição operacional, porque apresentou menor perda de carga residual para uma maior massa retida durante os 100 ciclos de filtração. Para as duas velocidades de filtração de 10 cm/s e 5 cm/s, o meio filtrante Rad Mais, mais poroso e mais permeável, a quantidade de massa de partículas removida foi maior quando comparado com o meio filtrante Rad Plus com Vl de 18cm/s, porque a força de remoção para a Vl de 18 cm/s conseguiu remover as partículas retidas nas fibras. Já para a Vf de 5 cm/s, uma menor velocidade de limpeza, Vl de 13 cm/s foi suficiente para remover maior quantidade de partículas, quando comparada com o meio filtrante Rad Plus nas mesmas condições experimentais.Universidade Federal de Sao Carlosapplication/pdfporUniversidade Federal de São CarlosPrograma de Pós-Graduação em Engenharia Química - PPGEQUFSCarBRFiltração de gasesMeios filtrantes de celulosePerda de carga residualPorosidadeENGENHARIAS::ENGENHARIA QUIMICAComportamento da filtração de gases em meios filtrantes de celulose.info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesis-1-1cfe199c5-37b6-4d5a-a38c-e0503b6b1995info:eu-repo/semantics/openAccessreponame:Repositório Institucional da UFSCARinstname:Universidade Federal de São Carlos (UFSCAR)instacron:UFSCARORIGINALDissVMO.pdfapplication/pdf4943436https://repositorio.ufscar.br/bitstream/ufscar/3977/1/DissVMO.pdf2211c87e5be0a702fd92e5103e1a5e1aMD51THUMBNAILDissVMO.pdf.jpgDissVMO.pdf.jpgIM Thumbnailimage/jpeg5715https://repositorio.ufscar.br/bitstream/ufscar/3977/2/DissVMO.pdf.jpg3d0b3ecc98df50df8263276d9e41e708MD52ufscar/39772023-09-18 18:31:40.162oai:repositorio.ufscar.br:ufscar/3977Repositório InstitucionalPUBhttps://repositorio.ufscar.br/oai/requestopendoar:43222023-09-18T18:31:40Repositório Institucional da UFSCAR - Universidade Federal de São Carlos (UFSCAR)false
dc.title.por.fl_str_mv Comportamento da filtração de gases em meios filtrantes de celulose.
title Comportamento da filtração de gases em meios filtrantes de celulose.
spellingShingle Comportamento da filtração de gases em meios filtrantes de celulose.
Osório, Vanessa Moreira
Filtração de gases
Meios filtrantes de celulose
Perda de carga residual
Porosidade
ENGENHARIAS::ENGENHARIA QUIMICA
title_short Comportamento da filtração de gases em meios filtrantes de celulose.
title_full Comportamento da filtração de gases em meios filtrantes de celulose.
title_fullStr Comportamento da filtração de gases em meios filtrantes de celulose.
title_full_unstemmed Comportamento da filtração de gases em meios filtrantes de celulose.
title_sort Comportamento da filtração de gases em meios filtrantes de celulose.
author Osório, Vanessa Moreira
author_facet Osório, Vanessa Moreira
author_role author
dc.contributor.authorlattes.por.fl_str_mv http://lattes.cnpq.br/3282723304057244
dc.contributor.author.fl_str_mv Osório, Vanessa Moreira
dc.contributor.advisor1.fl_str_mv Aguiar, Mônica Lopes
dc.contributor.advisor1Lattes.fl_str_mv http://lattes.cnpq.br/0431688649128529
dc.contributor.authorID.fl_str_mv 3a2fb3fd-e3c4-43ff-b195-c70800bd4645
contributor_str_mv Aguiar, Mônica Lopes
dc.subject.por.fl_str_mv Filtração de gases
Meios filtrantes de celulose
Perda de carga residual
Porosidade
topic Filtração de gases
Meios filtrantes de celulose
Perda de carga residual
Porosidade
ENGENHARIAS::ENGENHARIA QUIMICA
dc.subject.cnpq.fl_str_mv ENGENHARIAS::ENGENHARIA QUIMICA
description The present work aims to evaluate, through filtration process and cake detachment, the behavior of two cellulose fiber filtering media with different air permeability values. The powder material used was phosphatic concentrated rock of density 2,99 g/cm3 and its average volumetric diameter of 8,34 µm. The equipment used was constituted of a circular filter, powder feeder which controlled the massic flow and humidity by a microcomputer and a system for control and acquisition of data. The filtering media used were cellulose fibers, Rad More and Rad Plus, supplied by Alhstrom Louveira. The work was accomplished by a successive sequence of filtration and cleaning during 100 filtration cycles using cellulose filtering media. The technique employed for cake removal was reverse air flow. In the experimental procedure, filtration velocity of 10 cm/s was used for maximum pressure drop of 200 mmH2O, and 5 cm/s for maximum pressure drop of 100 mmH2O. Two cleaning velocity were employed for cake removal, 18 and 13 cm/s. The results showed that the filtering media Rad Plus, when submitted to filtration velocity of 10 cm/s and cleaning velocity of 18 cm/s, obtained the best operational condition, as it presented lower values of residual pressure drop for a larger mass retained during the 100 filtration cycles. For different filtration velocity, 10 and 5 cm/s, the filtering media Rad Plus, more porous and more permeable, the amount of particle mass removed was larger than for the filtering media Rad Plus applying cleaning velocity of 18cm/s as the removal force for this cleaning velocity could remove the particles retained in the fibers. For filtration velocity of 5 cm/s, a lower cleaning velocity, 13 cm/s, was enough to remove larger amount of particles, when compared with the filtering media Rad Plus in the same experimental conditions.
publishDate 2006
dc.date.issued.fl_str_mv 2006-09-15
dc.date.available.fl_str_mv 2007-10-19
2016-06-02T19:56:28Z
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dc.identifier.citation.fl_str_mv OSÓRIO, Vanessa Moreira. Comportamento da filtração de gases em meios filtrantes de celulose.. 2006. 133 f. Dissertação (Mestrado em Ciências Exatas e da Terra) - Universidade Federal de São Carlos, São Carlos, 2006.
dc.identifier.uri.fl_str_mv https://repositorio.ufscar.br/handle/ufscar/3977
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