Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad
Autor(a) principal: | |
---|---|
Data de Publicação: | 2017 |
Tipo de documento: | Dissertação |
Idioma: | por |
Título da fonte: | Biblioteca Digital de Teses e Dissertações da UNICAP |
Texto Completo: | http://tede2.unicap.br:8080/handle/tede/1051 |
Resumo: | A methodology was developed for the treatment of an effluent from the metalworking industry composed of water, cutting fluid and graphite. The recovery of components from an effluent from the machining process becomes complex due to the coexistence of solids such as graphite, mixed with a water-oil emulsion. Due to the use of graphite in very small particles and emulsified in water with the aid of an emulsifier, distributing in both phases (aqueous and organic), making the treatment process difficult. In general, treating such an effluent requires, in the preliminary step, the breaking of the emulsion so that the graphite dispersed in the liquid medium is recovered. The treatment was initially performed in a prototype phase separation in laboratory scale, counting on recirculation tanks, pumps, hydrocyclones and continuous decanter. In an initial stage the effluent was acidified by the addition of sulfuric acid PA as a way of breaking the solid-liquid emulsion. Subsequently, the solid phase was reered with the aid of a hydrocyclone, resulting in an overflow of the equipment of a mixture of water and residual oil. The mixture of part of the water and the water-cutting fluid, after acid destabilization of the emulsion, was separated into the continuous decanter, giving rise to a stream of cutting fluid and an aqueous phase containing residual oil, contaminated by about 130 ppm Of organic phase. The aqueous phase was then subjected to a dissolved air flotation (FAD) process, aided by a demulsifying biosurfactant in a FAD prototype, also on a laboratory scale. In order to define adequate conditions to obtain an aqueous phase with contamination level that allowed its return to the process, the operational conditions of application of the FAD technique were determined with the aid of an experimental design of the type rotational central compost (CDCR). At the end of the aqueous phase recovery process, a residual oil content of 12% was obtained, below that required by the Brazilian environmental regulatory agency (CONAMA) for discharge in water bodies, which is 20 ppm. The recoveries of graphite and cutting fluid are suggested studies for the next works. |
id |
UCAP_ba142100d26be54dc0b1ecce604f9bde |
---|---|
oai_identifier_str |
oai:tede2.unicap.br:tede/1051 |
network_acronym_str |
UCAP |
network_name_str |
Biblioteca Digital de Teses e Dissertações da UNICAP |
repository_id_str |
4646 |
spelling |
Santos, Valdemir Alexandre dos079.743.104-72http://lattes.cnpq.br/6361567059632670Sarubbo, Leonie Asfora735.801.634-34http://lattes.cnpq.br/4691045388698504Bernardino Junior, Francisco Madeiro430.471.653-00http://lattes.cnpq.br/1934903225521860Brandão, Yana Batista027.390.064-11http://lattes.cnpq.br/3860227097940599083.826.284-86http://lattes.cnpq.br/0510831736181686Santana, Renata Kelly de Lima2018-11-20T18:51:24Z2017-11-20SANTANA, Renata Kelly de Lima. Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad. 2017. 80 f Dissertação (Mestrado) - Universidade Católica de Pernambuco. Pró-reitoria Acadêmica. Coordenação Geral de Pós-graduação. Mestrado em Desenvolvimento de Processos Ambientais, 2017.http://tede2.unicap.br:8080/handle/tede/1051A methodology was developed for the treatment of an effluent from the metalworking industry composed of water, cutting fluid and graphite. The recovery of components from an effluent from the machining process becomes complex due to the coexistence of solids such as graphite, mixed with a water-oil emulsion. Due to the use of graphite in very small particles and emulsified in water with the aid of an emulsifier, distributing in both phases (aqueous and organic), making the treatment process difficult. In general, treating such an effluent requires, in the preliminary step, the breaking of the emulsion so that the graphite dispersed in the liquid medium is recovered. The treatment was initially performed in a prototype phase separation in laboratory scale, counting on recirculation tanks, pumps, hydrocyclones and continuous decanter. In an initial stage the effluent was acidified by the addition of sulfuric acid PA as a way of breaking the solid-liquid emulsion. Subsequently, the solid phase was reered with the aid of a hydrocyclone, resulting in an overflow of the equipment of a mixture of water and residual oil. The mixture of part of the water and the water-cutting fluid, after acid destabilization of the emulsion, was separated into the continuous decanter, giving rise to a stream of cutting fluid and an aqueous phase containing residual oil, contaminated by about 130 ppm Of organic phase. The aqueous phase was then subjected to a dissolved air flotation (FAD) process, aided by a demulsifying biosurfactant in a FAD prototype, also on a laboratory scale. In order to define adequate conditions to obtain an aqueous phase with contamination level that allowed its return to the process, the operational conditions of application of the FAD technique were determined with the aid of an experimental design of the type rotational central compost (CDCR). At the end of the aqueous phase recovery process, a residual oil content of 12% was obtained, below that required by the Brazilian environmental regulatory agency (CONAMA) for discharge in water bodies, which is 20 ppm. The recoveries of graphite and cutting fluid are suggested studies for the next works.Foi desenvolvida uma metodologia para tratamento de um efluente da indústria metalmecânica composto de água, fluido de corte e grafite. A recuperação de componentes de um efluente do processo de usinagem torna-se complexa devido à coexistência de sólidos como o grafite, misturado a uma emulsão do tipo água-óleo. Devido ao uso do grafite em partículas muito pequenas e emulsionado em água com auxílio de um emulsificante, distribuindo-se em ambas as fases (aquosa e orgânica), dificultando o processo de tratamento. De modo geral o tratamento de um efluente desse tipo exige, na etapa preliminar, a quebra da emulsão para que seja recuperado o grafite disperso no meio líquido. O tratamento foi inicialmente realizado em um protótipo de separação de fases em escala de laboratório, contando com tanques de recirculação, bombas, hidrociclones e decantador contínuo. Numa etapa inicial o efluente foi acidificado através da adição de ácido sulfúrico PA como forma de quebrar a emulsão sólido-líquido. Posteriormente, foi recuperada a fase sólida com auxílio de um hidrociclone, dando origem a uma descarga pelo overflow do equipamento de uma mistura de água e óleo de corte residual. A mistura de parte da água e do água-fluido de corte, após a desestabilização ácida da emulsão, foi separada no decantador contínuo, dando origem a uma corrente de fluido de corte e uma fase aquosa contendo óleo residual, contaminada por cerca de 130 ppm de fase orgânica. A fase aquosa foi então submetida a um processo de flotação por ar dissolvido (FAD), auxiliada por biossurfactante desemulsificante em um protótipo FAD, também em escala de laboratório. Para definir condições adequadas à obtenção de uma fase aquosa com nível de contaminação que permitisse seu retorno ao processo, as condições operacionais de aplicação da técnica de FAD foram determinadas com auxílio de um planejamento experimental do tipo Delineamento Compost Central Rotacional (DCCR). Ao final do processo de recuperação da fase aquosa foi obtido um teor óleo residual de 12 %, abaixo do exigido pelo órgão brasileiro de regulamentação ambiental (CONAMA) para descarte em corpos hídricos, que é de 20 ppm. As recuperações do grafite e do fluido de corte são estudos sugeridos para os próximos trabalhos.Submitted by Biblioteca Central (biblioteca@unicap.br) on 2018-11-20T18:51:24Z No. of bitstreams: 2 renata_kelly_lima_santana.pdf: 1101025 bytes, checksum: a6b7adb81731f8710c249fee6ad58062 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5)Made available in DSpace on 2018-11-20T18:51:24Z (GMT). No. of bitstreams: 2 renata_kelly_lima_santana.pdf: 1101025 bytes, checksum: a6b7adb81731f8710c249fee6ad58062 (MD5) license_rdf: 0 bytes, checksum: d41d8cd98f00b204e9800998ecf8427e (MD5) Previous issue date: 2017-11-20Coordenação de Aperfeiçoamento de Pessoal de Nível Superior - CAPESConselho Nacional de Pesquisa e Desenvolvimento Científico e Tecnológico - CNPqapplication/pdfporUniversidade Católica de PernambucoMestrado em Desenvolvimento de Processos AmbientaisUNICAPBrasilDepartamento de Pós-Graduaçãohttp://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessSeparação (Tecnologia)Água - ReutilizaçãoÁgua - PurificaçãoDissertaçõesDissertationsSeparation (Technology)Water - ReuseWater - PurificationCIENCIAS BIOLOGICAS::BIOLOGIA GERALTratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fadinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesis7773858030179640429500500600600600-8854052368273140835-16345593859312446972075167498588264571-2555911436985713659reponame:Biblioteca Digital de Teses e Dissertações da UNICAPinstname:Universidade Católica de Pernambuco (UNICAP)instacron:UNICAPORIGINALrenata_kelly_lima_santana.pdfrenata_kelly_lima_santana.pdfapplication/pdf1101025http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/5/renata_kelly_lima_santana.pdfa6b7adb81731f8710c249fee6ad58062MD55CC-LICENSElicense_urllicense_urltext/plain; charset=utf-849http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/2/license_url4afdbb8c545fd630ea7db775da747b2fMD52license_textlicense_texttext/html; charset=utf-80http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/3/license_textd41d8cd98f00b204e9800998ecf8427eMD53license_rdflicense_rdfapplication/rdf+xml; charset=utf-80http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/4/license_rdfd41d8cd98f00b204e9800998ecf8427eMD54LICENSElicense.txtlicense.txttext/plain; charset=utf-82170http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/1/license.txt5d71329502a0e313f28be890c62f4ad8MD51tede/10512018-11-20 16:51:24.582oai:tede2.unicap.br: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Biblioteca Digital de Teses e Dissertaçõeshttp://tede2.unicap.br:8080/http://tede2.unicap.br:8080/oai/requestbiblioteca@unicap.br||biblioteca@unicap.bropendoar:46462018-11-20T18:51:24Biblioteca Digital de Teses e Dissertações da UNICAP - Universidade Católica de Pernambuco (UNICAP)false |
dc.title.por.fl_str_mv |
Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad |
title |
Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad |
spellingShingle |
Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad Santana, Renata Kelly de Lima Separação (Tecnologia) Água - Reutilização Água - Purificação Dissertações Dissertations Separation (Technology) Water - Reuse Water - Purification CIENCIAS BIOLOGICAS::BIOLOGIA GERAL |
title_short |
Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad |
title_full |
Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad |
title_fullStr |
Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad |
title_full_unstemmed |
Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad |
title_sort |
Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad |
author |
Santana, Renata Kelly de Lima |
author_facet |
Santana, Renata Kelly de Lima |
author_role |
author |
dc.contributor.advisor1.fl_str_mv |
Santos, Valdemir Alexandre dos |
dc.contributor.advisor1ID.fl_str_mv |
079.743.104-72 |
dc.contributor.advisor1Lattes.fl_str_mv |
http://lattes.cnpq.br/6361567059632670 |
dc.contributor.advisor-co1.fl_str_mv |
Sarubbo, Leonie Asfora |
dc.contributor.advisor-co1ID.fl_str_mv |
735.801.634-34 |
dc.contributor.advisor-co1Lattes.fl_str_mv |
http://lattes.cnpq.br/4691045388698504 |
dc.contributor.referee1.fl_str_mv |
Bernardino Junior, Francisco Madeiro |
dc.contributor.referee1ID.fl_str_mv |
430.471.653-00 |
dc.contributor.referee1Lattes.fl_str_mv |
http://lattes.cnpq.br/1934903225521860 |
dc.contributor.referee2.fl_str_mv |
Brandão, Yana Batista |
dc.contributor.referee2ID.fl_str_mv |
027.390.064-11 |
dc.contributor.referee2Lattes.fl_str_mv |
http://lattes.cnpq.br/3860227097940599 |
dc.contributor.authorID.fl_str_mv |
083.826.284-86 |
dc.contributor.authorLattes.fl_str_mv |
http://lattes.cnpq.br/0510831736181686 |
dc.contributor.author.fl_str_mv |
Santana, Renata Kelly de Lima |
contributor_str_mv |
Santos, Valdemir Alexandre dos Sarubbo, Leonie Asfora Bernardino Junior, Francisco Madeiro Brandão, Yana Batista |
dc.subject.por.fl_str_mv |
Separação (Tecnologia) Água - Reutilização Água - Purificação Dissertações |
topic |
Separação (Tecnologia) Água - Reutilização Água - Purificação Dissertações Dissertations Separation (Technology) Water - Reuse Water - Purification CIENCIAS BIOLOGICAS::BIOLOGIA GERAL |
dc.subject.eng.fl_str_mv |
Dissertations Separation (Technology) Water - Reuse Water - Purification |
dc.subject.cnpq.fl_str_mv |
CIENCIAS BIOLOGICAS::BIOLOGIA GERAL |
description |
A methodology was developed for the treatment of an effluent from the metalworking industry composed of water, cutting fluid and graphite. The recovery of components from an effluent from the machining process becomes complex due to the coexistence of solids such as graphite, mixed with a water-oil emulsion. Due to the use of graphite in very small particles and emulsified in water with the aid of an emulsifier, distributing in both phases (aqueous and organic), making the treatment process difficult. In general, treating such an effluent requires, in the preliminary step, the breaking of the emulsion so that the graphite dispersed in the liquid medium is recovered. The treatment was initially performed in a prototype phase separation in laboratory scale, counting on recirculation tanks, pumps, hydrocyclones and continuous decanter. In an initial stage the effluent was acidified by the addition of sulfuric acid PA as a way of breaking the solid-liquid emulsion. Subsequently, the solid phase was reered with the aid of a hydrocyclone, resulting in an overflow of the equipment of a mixture of water and residual oil. The mixture of part of the water and the water-cutting fluid, after acid destabilization of the emulsion, was separated into the continuous decanter, giving rise to a stream of cutting fluid and an aqueous phase containing residual oil, contaminated by about 130 ppm Of organic phase. The aqueous phase was then subjected to a dissolved air flotation (FAD) process, aided by a demulsifying biosurfactant in a FAD prototype, also on a laboratory scale. In order to define adequate conditions to obtain an aqueous phase with contamination level that allowed its return to the process, the operational conditions of application of the FAD technique were determined with the aid of an experimental design of the type rotational central compost (CDCR). At the end of the aqueous phase recovery process, a residual oil content of 12% was obtained, below that required by the Brazilian environmental regulatory agency (CONAMA) for discharge in water bodies, which is 20 ppm. The recoveries of graphite and cutting fluid are suggested studies for the next works. |
publishDate |
2017 |
dc.date.issued.fl_str_mv |
2017-11-20 |
dc.date.accessioned.fl_str_mv |
2018-11-20T18:51:24Z |
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 |
SANTANA, Renata Kelly de Lima. Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad. 2017. 80 f Dissertação (Mestrado) - Universidade Católica de Pernambuco. Pró-reitoria Acadêmica. Coordenação Geral de Pós-graduação. Mestrado em Desenvolvimento de Processos Ambientais, 2017. |
dc.identifier.uri.fl_str_mv |
http://tede2.unicap.br:8080/handle/tede/1051 |
identifier_str_mv |
SANTANA, Renata Kelly de Lima. Tratamento de águas oleosas com alto grau de emulsificação e presença de sólidos de baixa densidade utilizando fad. 2017. 80 f Dissertação (Mestrado) - Universidade Católica de Pernambuco. Pró-reitoria Acadêmica. Coordenação Geral de Pós-graduação. Mestrado em Desenvolvimento de Processos Ambientais, 2017. |
url |
http://tede2.unicap.br:8080/handle/tede/1051 |
dc.language.iso.fl_str_mv |
por |
language |
por |
dc.relation.program.fl_str_mv |
7773858030179640429 |
dc.relation.confidence.fl_str_mv |
500 500 600 600 600 |
dc.relation.department.fl_str_mv |
-8854052368273140835 |
dc.relation.cnpq.fl_str_mv |
-1634559385931244697 |
dc.relation.sponsorship.fl_str_mv |
2075167498588264571 -2555911436985713659 |
dc.rights.driver.fl_str_mv |
http://creativecommons.org/licenses/by-nc-nd/4.0/ info:eu-repo/semantics/openAccess |
rights_invalid_str_mv |
http://creativecommons.org/licenses/by-nc-nd/4.0/ |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
application/pdf |
dc.publisher.none.fl_str_mv |
Universidade Católica de Pernambuco |
dc.publisher.program.fl_str_mv |
Mestrado em Desenvolvimento de Processos Ambientais |
dc.publisher.initials.fl_str_mv |
UNICAP |
dc.publisher.country.fl_str_mv |
Brasil |
dc.publisher.department.fl_str_mv |
Departamento de Pós-Graduação |
publisher.none.fl_str_mv |
Universidade Católica de Pernambuco |
dc.source.none.fl_str_mv |
reponame:Biblioteca Digital de Teses e Dissertações da UNICAP instname:Universidade Católica de Pernambuco (UNICAP) instacron:UNICAP |
instname_str |
Universidade Católica de Pernambuco (UNICAP) |
instacron_str |
UNICAP |
institution |
UNICAP |
reponame_str |
Biblioteca Digital de Teses e Dissertações da UNICAP |
collection |
Biblioteca Digital de Teses e Dissertações da UNICAP |
bitstream.url.fl_str_mv |
http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/5/renata_kelly_lima_santana.pdf http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/2/license_url http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/3/license_text http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/4/license_rdf http://tede2.unicap.br:8080/handle/tede/bitstream/tede/1051/1/license.txt |
bitstream.checksum.fl_str_mv |
a6b7adb81731f8710c249fee6ad58062 4afdbb8c545fd630ea7db775da747b2f d41d8cd98f00b204e9800998ecf8427e d41d8cd98f00b204e9800998ecf8427e 5d71329502a0e313f28be890c62f4ad8 |
bitstream.checksumAlgorithm.fl_str_mv |
MD5 MD5 MD5 MD5 MD5 |
repository.name.fl_str_mv |
Biblioteca Digital de Teses e Dissertações da UNICAP - Universidade Católica de Pernambuco (UNICAP) |
repository.mail.fl_str_mv |
biblioteca@unicap.br||biblioteca@unicap.br |
_version_ |
1811737520230105088 |