Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos
Autor(a) principal: | |
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Data de Publicação: | 2014 |
Tipo de documento: | Tese |
Idioma: | por |
Título da fonte: | Repositório Institucional da UFRN |
Texto Completo: | https://repositorio.ufrn.br/jspui/handle/123456789/17785 |
Resumo: | The environmental impact due to the improper disposal of metal-bearing industrial effluents imposes the need of wastewater treatment, since heavy metals are nonbiodegradable and hazardous substances that may cause undesirable effects to humans and the environment. The use of microemulsion systems for the extraction of metal ions from wastewaters is effective when it occurs in a Winsor II (WII) domain, where a microemulsion phase is in equilibrium with an aqueous phase in excess. However, the microemulsion phase formed in this system has a higher amount of active matter when compared to a WIII system (microemulsion in equilibrium with aqueous and oil phases both in excess). This was the reason to develop a comparative study to evaluate the efficiency of two-phases and three-phases microemulsion systems (WII and WIII) in the extraction of Cu+2 and Ni+2 from aqueous solutions. The systems were composed by: saponified coconut oil (SCO) as surfactant, n-Butanol as cosurfactant, kerosene as oil phase, and synthetic solutions of CuSO4.5H2O and NiSO4.6H2O, with 2 wt.% NaCl, as aqueous phase. Pseudoternary phase diagrams were obtained and the systems were characterized by using surface tension measurements, particle size determination and scanning electron microscopy (SEM). The concentrations of metal ions before and after extraction were determined by atomic absorption spectrometry. The extraction study of Cu+2 and Ni+2 in the WIII domain contributed to a better understanding of microemulsion extraction, elucidating the various behaviors presented in the literature for these systems. Furthermore, since WIII systems presented high extraction efficiencies, similar to the ones presented by Winsor II systems, they represented an economic and technological advantage in heavy metal extraction due to a small amount of surfactant and cosurfactant used in the process and also due to the formation of a reduced volume of aqueous phase, with high concentration of metal. Considering the reextraction process, it was observed that WIII system is more effective because it is performed in the oil phase, unlike reextraction in WII, which is performed in the aqueous phase. The presence of the metalsurfactant complex in the oil phase makes possible to regenerate only the surfactant present in the organic phase, and not all the surfactant in the process, as in WII system. This fact allows the reuse of the microemulsion phase in a new extraction process, reducing the costs with surfactant regeneration |
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Oliveira, Mônica Rodrigues dehttp://lattes.cnpq.br/2219717055055892http://lattes.cnpq.br/0676872399141537Silva, Djalma Ribeiro dahttp://lattes.cnpq.br/2791074318745945Barros Neto, Eduardo Lins dehttp://lattes.cnpq.br/2811639726261017Peres, Antônio Eduardo Clarkhttp://lattes.cnpq.br/8666548473150908Lucena Neto, Marciano Henrique dehttp://lattes.cnpq.br/4809804711785369Dantas, Tereza Neuma de Castro2014-12-17T15:42:28Z2014-04-162014-12-17T15:42:28Z2014-01-23OLIVEIRA, Mônica Rodrigues de. Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos. 2014. 130 f. Tese (Doutorado em Físico-Química; Química) - Universidade Federal do Rio Grande do Norte, Natal, 2014.https://repositorio.ufrn.br/jspui/handle/123456789/17785The environmental impact due to the improper disposal of metal-bearing industrial effluents imposes the need of wastewater treatment, since heavy metals are nonbiodegradable and hazardous substances that may cause undesirable effects to humans and the environment. The use of microemulsion systems for the extraction of metal ions from wastewaters is effective when it occurs in a Winsor II (WII) domain, where a microemulsion phase is in equilibrium with an aqueous phase in excess. However, the microemulsion phase formed in this system has a higher amount of active matter when compared to a WIII system (microemulsion in equilibrium with aqueous and oil phases both in excess). This was the reason to develop a comparative study to evaluate the efficiency of two-phases and three-phases microemulsion systems (WII and WIII) in the extraction of Cu+2 and Ni+2 from aqueous solutions. The systems were composed by: saponified coconut oil (SCO) as surfactant, n-Butanol as cosurfactant, kerosene as oil phase, and synthetic solutions of CuSO4.5H2O and NiSO4.6H2O, with 2 wt.% NaCl, as aqueous phase. Pseudoternary phase diagrams were obtained and the systems were characterized by using surface tension measurements, particle size determination and scanning electron microscopy (SEM). The concentrations of metal ions before and after extraction were determined by atomic absorption spectrometry. The extraction study of Cu+2 and Ni+2 in the WIII domain contributed to a better understanding of microemulsion extraction, elucidating the various behaviors presented in the literature for these systems. Furthermore, since WIII systems presented high extraction efficiencies, similar to the ones presented by Winsor II systems, they represented an economic and technological advantage in heavy metal extraction due to a small amount of surfactant and cosurfactant used in the process and also due to the formation of a reduced volume of aqueous phase, with high concentration of metal. Considering the reextraction process, it was observed that WIII system is more effective because it is performed in the oil phase, unlike reextraction in WII, which is performed in the aqueous phase. The presence of the metalsurfactant complex in the oil phase makes possible to regenerate only the surfactant present in the organic phase, and not all the surfactant in the process, as in WII system. This fact allows the reuse of the microemulsion phase in a new extraction process, reducing the costs with surfactant regenerationO impacto ambiental gerado pelo descarte de efluentes industriais carregados de metais pesados impõe a necessidade do tratamento desses rejeitos, uma vez que são tóxicos e não biodegradáveis, podendo causar sérios danos à população e ao meio ambiente. O processo de extração de cátions metálicos utilizando microemulsões é eficaz quando acontece em WII, onde a fase microemulsionada encontra-se em equilíbrio com uma fase aquosa em excesso. No entanto, a microemulsão formada nesse sistema possui uma maior quantidade de matéria ativa quando comparada ao equilíbrio de WIII (microemulsão em equilíbrio com fases aquosa e oleosa, ambas em excesso), ainda pouco estudado, motivando, assim, o desenvolvimento de um estudo comparativo da eficiência de extração dos íons Cu2+ e Ni2+ por sistemas microemulsionados bifásicos e trifásicos (WII e WIII). Os constituintes utilizados nos sistemas de extração foram: óleo de coco saponificado - OCS (Tensoativo), n- Butanol (Cotensoativo), querosene (Fase Oleosa) e soluções sintéticas de CuSO4.5H2O e NiSO4.6H2O com NaCl 2% (fases aquosas). Foram obtidos os diagramas de fases pseudoternários e os sistemas microemulsionados foram caracterizados através das técnicas de tensão superficial, tamanho de partículas e microscopia eletrônica de varredura (MEV). A concentração dos íons foi determinada por espectrometria de absorção atômica. O estudo da extração dos cátions metálicos Cu2+ e Ni2+ na região de WIII contribuiu para um melhor entendimento dos processos de extração por microemulsão, elucidando os vários comportamentos apresentados na literatura para esses sistemas. Além disso, uma vez que houve uma alta eficiência de extração, similar aos sistemas de Winsor II, o sistema trifásico (WIII), por apresentar uma menor quantidade de tensoativo e cotensoativo, e um menor volume de fase aquosa após a extração, levou a uma maior concentração do metal, representando uma vantagem econômica e tecnológica do processo. Assim, a extração em sistema trifásico é viável e, apesar dos percentuais de extração em WII e WIII serem semelhantes, o sistema de WIII leva a uma maior concentração do metal na fase extrato. O presente trabalho mostrou, ainda, que a etapa de reextração para os sistemas em WIII é mais eficaz pois, diferentemente da extração em Winsor II, ela é realizada na fase oleosa, onde está depositado o complexo metal/tensoativo, regenerando somente o tensoativo que complexa com o metal na fase orgânica, e não todo o tensoativo utilizado, como é o caso do equilíbrio em Winsor II. Este fato viabiliza a reutilização da fase microemulsão no processo de extração, diminuindo os custos de regeneração do tensoativoapplication/pdfporUniversidade Federal do Rio Grande do NortePrograma de Pós-Graduação em QuímicaUFRNBRFísico-Química; QuímicaExtração. Cobre. Níquel. Microemulsão. Winsor II. Winsor IIIExtraction. Copper. Nickel. Microemulsion. Winsor II. Winsor IIICNPQ::CIENCIAS EXATAS E DA TERRA::QUIMICAEficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicosinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/doctoralThesisinfo:eu-repo/semantics/openAccessreponame:Repositório Institucional da UFRNinstname:Universidade Federal do Rio Grande do Norte (UFRN)instacron:UFRNORIGINALMonicaRO_TESE.pdfapplication/pdf4155777https://repositorio.ufrn.br/bitstream/123456789/17785/1/MonicaRO_TESE.pdf6bff63b5cb0f37e64dfe6fcb144dae79MD51TEXTMonicaRO_TESE.pdf.txtMonicaRO_TESE.pdf.txtExtracted texttext/plain221138https://repositorio.ufrn.br/bitstream/123456789/17785/6/MonicaRO_TESE.pdf.txt0c5e8894edfe4e22749fb960a3f7b1f5MD56THUMBNAILMonicaRO_TESE.pdf.jpgMonicaRO_TESE.pdf.jpgIM Thumbnailimage/jpeg5512https://repositorio.ufrn.br/bitstream/123456789/17785/7/MonicaRO_TESE.pdf.jpgf1c24ede3a4210770bb1133ba095b116MD57123456789/177852017-11-04 14:42:48.838oai:https://repositorio.ufrn.br:123456789/17785Repositório de PublicaçõesPUBhttp://repositorio.ufrn.br/oai/opendoar:2017-11-04T17:42:48Repositório Institucional da UFRN - Universidade Federal do Rio Grande do Norte (UFRN)false |
dc.title.por.fl_str_mv |
Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos |
title |
Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos |
spellingShingle |
Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos Oliveira, Mônica Rodrigues de Extração. Cobre. Níquel. Microemulsão. Winsor II. Winsor III Extraction. Copper. Nickel. Microemulsion. Winsor II. Winsor III CNPQ::CIENCIAS EXATAS E DA TERRA::QUIMICA |
title_short |
Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos |
title_full |
Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos |
title_fullStr |
Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos |
title_full_unstemmed |
Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos |
title_sort |
Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos |
author |
Oliveira, Mônica Rodrigues de |
author_facet |
Oliveira, Mônica Rodrigues de |
author_role |
author |
dc.contributor.authorID.por.fl_str_mv |
|
dc.contributor.authorLattes.por.fl_str_mv |
http://lattes.cnpq.br/2219717055055892 |
dc.contributor.advisorID.por.fl_str_mv |
|
dc.contributor.advisorLattes.por.fl_str_mv |
http://lattes.cnpq.br/0676872399141537 |
dc.contributor.referees1.pt_BR.fl_str_mv |
Silva, Djalma Ribeiro da |
dc.contributor.referees1ID.por.fl_str_mv |
|
dc.contributor.referees1Lattes.por.fl_str_mv |
http://lattes.cnpq.br/2791074318745945 |
dc.contributor.referees2.pt_BR.fl_str_mv |
Barros Neto, Eduardo Lins de |
dc.contributor.referees2ID.por.fl_str_mv |
|
dc.contributor.referees2Lattes.por.fl_str_mv |
http://lattes.cnpq.br/2811639726261017 |
dc.contributor.referees3.pt_BR.fl_str_mv |
Peres, Antônio Eduardo Clark |
dc.contributor.referees3ID.por.fl_str_mv |
|
dc.contributor.referees3Lattes.por.fl_str_mv |
http://lattes.cnpq.br/8666548473150908 |
dc.contributor.referees4.pt_BR.fl_str_mv |
Lucena Neto, Marciano Henrique de |
dc.contributor.referees4ID.por.fl_str_mv |
|
dc.contributor.referees4Lattes.por.fl_str_mv |
http://lattes.cnpq.br/4809804711785369 |
dc.contributor.author.fl_str_mv |
Oliveira, Mônica Rodrigues de |
dc.contributor.advisor1.fl_str_mv |
Dantas, Tereza Neuma de Castro |
contributor_str_mv |
Dantas, Tereza Neuma de Castro |
dc.subject.por.fl_str_mv |
Extração. Cobre. Níquel. Microemulsão. Winsor II. Winsor III |
topic |
Extração. Cobre. Níquel. Microemulsão. Winsor II. Winsor III Extraction. Copper. Nickel. Microemulsion. Winsor II. Winsor III CNPQ::CIENCIAS EXATAS E DA TERRA::QUIMICA |
dc.subject.eng.fl_str_mv |
Extraction. Copper. Nickel. Microemulsion. Winsor II. Winsor III |
dc.subject.cnpq.fl_str_mv |
CNPQ::CIENCIAS EXATAS E DA TERRA::QUIMICA |
description |
The environmental impact due to the improper disposal of metal-bearing industrial effluents imposes the need of wastewater treatment, since heavy metals are nonbiodegradable and hazardous substances that may cause undesirable effects to humans and the environment. The use of microemulsion systems for the extraction of metal ions from wastewaters is effective when it occurs in a Winsor II (WII) domain, where a microemulsion phase is in equilibrium with an aqueous phase in excess. However, the microemulsion phase formed in this system has a higher amount of active matter when compared to a WIII system (microemulsion in equilibrium with aqueous and oil phases both in excess). This was the reason to develop a comparative study to evaluate the efficiency of two-phases and three-phases microemulsion systems (WII and WIII) in the extraction of Cu+2 and Ni+2 from aqueous solutions. The systems were composed by: saponified coconut oil (SCO) as surfactant, n-Butanol as cosurfactant, kerosene as oil phase, and synthetic solutions of CuSO4.5H2O and NiSO4.6H2O, with 2 wt.% NaCl, as aqueous phase. Pseudoternary phase diagrams were obtained and the systems were characterized by using surface tension measurements, particle size determination and scanning electron microscopy (SEM). The concentrations of metal ions before and after extraction were determined by atomic absorption spectrometry. The extraction study of Cu+2 and Ni+2 in the WIII domain contributed to a better understanding of microemulsion extraction, elucidating the various behaviors presented in the literature for these systems. Furthermore, since WIII systems presented high extraction efficiencies, similar to the ones presented by Winsor II systems, they represented an economic and technological advantage in heavy metal extraction due to a small amount of surfactant and cosurfactant used in the process and also due to the formation of a reduced volume of aqueous phase, with high concentration of metal. Considering the reextraction process, it was observed that WIII system is more effective because it is performed in the oil phase, unlike reextraction in WII, which is performed in the aqueous phase. The presence of the metalsurfactant complex in the oil phase makes possible to regenerate only the surfactant present in the organic phase, and not all the surfactant in the process, as in WII system. This fact allows the reuse of the microemulsion phase in a new extraction process, reducing the costs with surfactant regeneration |
publishDate |
2014 |
dc.date.accessioned.fl_str_mv |
2014-12-17T15:42:28Z |
dc.date.available.fl_str_mv |
2014-04-16 2014-12-17T15:42:28Z |
dc.date.issued.fl_str_mv |
2014-01-23 |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/doctoralThesis |
format |
doctoralThesis |
status_str |
publishedVersion |
dc.identifier.citation.fl_str_mv |
OLIVEIRA, Mônica Rodrigues de. Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos. 2014. 130 f. Tese (Doutorado em Físico-Química; Química) - Universidade Federal do Rio Grande do Norte, Natal, 2014. |
dc.identifier.uri.fl_str_mv |
https://repositorio.ufrn.br/jspui/handle/123456789/17785 |
identifier_str_mv |
OLIVEIRA, Mônica Rodrigues de. Eficiência de extração de cobre e níquel utilizando sistemas microemulsionados bifásicos e trifásicos. 2014. 130 f. Tese (Doutorado em Físico-Química; Química) - Universidade Federal do Rio Grande do Norte, Natal, 2014. |
url |
https://repositorio.ufrn.br/jspui/handle/123456789/17785 |
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por |
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Universidade Federal do Rio Grande do Norte |
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Programa de Pós-Graduação em Química |
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UFRN |
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BR |
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Físico-Química; Química |
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Universidade Federal do Rio Grande do Norte |
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