Comportamento da filtração de gases em meios filtrantes de celulose.
Autor(a) principal: | |
---|---|
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. |
id |
SCAR_38834e751bbb04e4f80338830a659589 |
---|---|
oai_identifier_str |
oai:repositorio.ufscar.br:ufscar/3977 |
network_acronym_str |
SCAR |
network_name_str |
Repositório Institucional da UFSCAR |
repository_id_str |
4322 |
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 |
dc.date.accessioned.fl_str_mv |
2016-06-02T19:56:28Z |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/masterThesis |
format |
masterThesis |
status_str |
publishedVersion |
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 |
identifier_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. |
url |
https://repositorio.ufscar.br/handle/ufscar/3977 |
dc.language.iso.fl_str_mv |
por |
language |
por |
dc.relation.confidence.fl_str_mv |
-1 -1 |
dc.relation.authority.fl_str_mv |
cfe199c5-37b6-4d5a-a38c-e0503b6b1995 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
application/pdf |
dc.publisher.none.fl_str_mv |
Universidade Federal de São Carlos |
dc.publisher.program.fl_str_mv |
Programa de Pós-Graduação em Engenharia Química - PPGEQ |
dc.publisher.initials.fl_str_mv |
UFSCar |
dc.publisher.country.fl_str_mv |
BR |
publisher.none.fl_str_mv |
Universidade Federal de São Carlos |
dc.source.none.fl_str_mv |
reponame:Repositório Institucional da UFSCAR instname:Universidade Federal de São Carlos (UFSCAR) instacron:UFSCAR |
instname_str |
Universidade Federal de São Carlos (UFSCAR) |
instacron_str |
UFSCAR |
institution |
UFSCAR |
reponame_str |
Repositório Institucional da UFSCAR |
collection |
Repositório Institucional da UFSCAR |
bitstream.url.fl_str_mv |
https://repositorio.ufscar.br/bitstream/ufscar/3977/1/DissVMO.pdf https://repositorio.ufscar.br/bitstream/ufscar/3977/2/DissVMO.pdf.jpg |
bitstream.checksum.fl_str_mv |
2211c87e5be0a702fd92e5103e1a5e1a 3d0b3ecc98df50df8263276d9e41e708 |
bitstream.checksumAlgorithm.fl_str_mv |
MD5 MD5 |
repository.name.fl_str_mv |
Repositório Institucional da UFSCAR - Universidade Federal de São Carlos (UFSCAR) |
repository.mail.fl_str_mv |
|
_version_ |
1813715532024643584 |