Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono
| Ano de defesa: | 2025 |
|---|---|
| Autor(a) principal: | |
| Orientador(a): | |
| Banca de defesa: | |
| Tipo de documento: | Dissertação |
| Tipo de acesso: | Acesso aberto |
| Idioma: | por |
| Instituição de defesa: |
Universidade Federal de Minas Gerais
|
| Programa de Pós-Graduação: |
Não Informado pela instituição
|
| Departamento: |
Não Informado pela instituição
|
| País: |
Não Informado pela instituição
|
| Palavras-chave em Português: | |
| Link de acesso: | https://hdl.handle.net/1843/80523 |
Resumo: | Magnesium oxides and hydroxides have several technological applications and are important raw materials for several industrial sectors. Currently, these compounds are obtained mainly by thermal decomposition of magnesite (MgCO3), which requires high energy consumption and releases large amounts of CO2, one of the main greenhouse gases (GHGs). In this picture, an advantageous alternative is the use of serpentinite rock, which is a highly available source of non-carbonated magnesium in the world. Thus, in this work, two acidic routes were developed to obtain magnesium hydroxide from serpentinite (aqueous and thermal routes). In the aqueous route, sulfuric and hydrochloric acids were tested as leaching agents, while in the thermal route, ammonium sulfate was used. Both routes were divided into 3 main stages, characterized by the production of solids 1, 2 and 3. The influence of the parameters of temperature, reaction time and amount of leaching agent was studied considering as reference the efficiency in the extraction of magnesium from serpentinite. In the aqueous route, experiments were carried out at 3 scales – 80 mL, 1 L and 5 L, reaching a maximum magnesium extraction efficiency of 79%, with a magnesium recovery as Mg(OH)2 of 82%. Analyses by XRF showed the production of Mg(OH)2 with purities between 94-97% of MgO. In the thermal route, the efficiency in the extraction of magnesium from serpentinite was 86% and the recovery of magnesium as Mg(OH)2 was 39% with a purity of 84% of MgO, analyzed by SEM/EDS. The use of serpentinite to obtain magnesium hydroxide proved to be promising, since, from routes with low energy demand that presented satisfactory magnesium extraction efficiencies, it was possible to obtain Mg(OH)2 of high purity. |
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2025-02-28T19:32:59Z2025-09-09T00:19:07Z2025-02-28T19:32:59Z2025-01-22https://hdl.handle.net/1843/80523Magnesium oxides and hydroxides have several technological applications and are important raw materials for several industrial sectors. Currently, these compounds are obtained mainly by thermal decomposition of magnesite (MgCO3), which requires high energy consumption and releases large amounts of CO2, one of the main greenhouse gases (GHGs). In this picture, an advantageous alternative is the use of serpentinite rock, which is a highly available source of non-carbonated magnesium in the world. Thus, in this work, two acidic routes were developed to obtain magnesium hydroxide from serpentinite (aqueous and thermal routes). In the aqueous route, sulfuric and hydrochloric acids were tested as leaching agents, while in the thermal route, ammonium sulfate was used. Both routes were divided into 3 main stages, characterized by the production of solids 1, 2 and 3. The influence of the parameters of temperature, reaction time and amount of leaching agent was studied considering as reference the efficiency in the extraction of magnesium from serpentinite. In the aqueous route, experiments were carried out at 3 scales – 80 mL, 1 L and 5 L, reaching a maximum magnesium extraction efficiency of 79%, with a magnesium recovery as Mg(OH)2 of 82%. Analyses by XRF showed the production of Mg(OH)2 with purities between 94-97% of MgO. In the thermal route, the efficiency in the extraction of magnesium from serpentinite was 86% and the recovery of magnesium as Mg(OH)2 was 39% with a purity of 84% of MgO, analyzed by SEM/EDS. The use of serpentinite to obtain magnesium hydroxide proved to be promising, since, from routes with low energy demand that presented satisfactory magnesium extraction efficiencies, it was possible to obtain Mg(OH)2 of high purity.FAPEMIG - Fundação de Amparo à Pesquisa do Estado de Minas GeraisporUniversidade Federal de Minas Geraishttp://creativecommons.org/licenses/by-nc-nd/3.0/pt/info:eu-repo/semantics/openAccesshidróxido de magnésioserpentinitoaplicações tecnológicaspegada de carbonoQuímica inorgânicaHidróxido de magnésioSerpentina (Mineralogia)Inovações tecnológicasTermogravimetriaFluorescência de raio XRaios X – DifraçãoMicroscopia eletrônica de varreduraEspectroscopia de raio XTransformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbonoinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesisInglidy Silva Oliveirareponame:Repositório Institucional da UFMGinstname:Universidade Federal de Minas Gerais (UFMG)instacron:UFMGhttp://lattes.cnpq.br/9700287484979718Ana Paula de Carvalho Teixeirahttp://lattes.cnpq.br/0157609658246739Rochel Montero LagoFernando Soares LameirasFlavia Cristina Camilo MouraÓxidos e hidróxidos de magnésio possuem várias aplicações tecnológicas, constituindo importantes matérias primas para diversos setores industriais. Atualmente, esses compostos são obtidos principalmente pela decomposição térmica da magnesita (MgCO3), que demanda alto consumo de energia e libera grandes quantidades de CO2, um dos principais gases de efeito estufa (GEE). Neste cenário, uma alternativa vantajosa é o uso da rocha serpentinito, que é uma fonte de magnésio não carbonatada altamente disponível no mundo. Assim, neste trabalho foram otimizadas duas rotas ácidas para a obtenção de hidróxido de magnésio a partir do serpentinito (rotas aquosa e térmica). Na rota aquosa foram testados os ácidos sulfúrico e clorídrico como agentes lixiviantes, enquanto na rota térmica foi utilizado o sulfato de amônio. Ambas as rotas foram divididas em 3 etapas principais, caracterizadas pela obtenção dos sólidos 1, 2 e 3 e a influência dos parâmetros de temperatura, tempo de reação e quantidade de agente lixiviante foi estudada considerando-se como referência a eficiência na extração de magnésio do serpentinito. Na rota aquosa foram realizados experimentos em 3 escalas – 80 mL, 1 L e 5 L chegando à eficiência máxima na extração de magnésio de 79%, com uma recuperação de magnésio na forma de Mg(OH)2 de 82%. Análises por FRX mostraram a produção de Mg(OH)2 com purezas entre 94-97% de MgO. Já na rota térmica, a eficiência na extração de magnésio do serpentinito foi de 86% e a recuperação de magnésio como Mg(OH)2 foi de 39% com pureza de 84% de MgO, analisada por MEV/EDS. O uso do serpentinito para obtenção de hidróxido de magnésio se mostrou promissor, pois, a partir de rotas com baixa demanda de energia que apresentaram eficiências na extração de magnésio satisfatórias foi possível a obtenção de Mg(OH)2 de pureza elevada.BrasilICEX - INSTITUTO DE CIÊNCIAS EXATASPrograma de Pós-Graduação em QuímicaUFMGORIGINALDissertação Mestrado - Inglidy Oliveira_PDFa.pdfapplication/pdf6602104https://repositorio.ufmg.br//bitstreams/a6106dde-0d31-43bb-9f3d-4bd5620e0a11/download6b695a2c8b3e93c0f1010a3484dc17e1MD51trueAnonymousREADCC-LICENSElicense_rdfapplication/octet-stream811https://repositorio.ufmg.br//bitstreams/4f5fd6b0-fb53-4571-a1c5-cbfa1c4ea0e2/downloadcfd6801dba008cb6adbd9838b81582abMD52falseAnonymousREADLICENSElicense.txttext/plain2118https://repositorio.ufmg.br//bitstreams/a12a5a35-45f7-469c-b693-d34b2f9ad40e/downloadcda590c95a0b51b4d15f60c9642ca272MD53falseAnonymousREAD1843/805232025-09-08 21:19:07.504http://creativecommons.org/licenses/by-nc-nd/3.0/pt/Acesso Abertoopen.accessoai:repositorio.ufmg.br:1843/80523https://repositorio.ufmg.br/Repositório InstitucionalPUBhttps://repositorio.ufmg.br/oairepositorio@ufmg.bropendoar:2025-09-09T00:19:07Repositório Institucional da UFMG - Universidade Federal de Minas Gerais (UFMG)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 |
| dc.title.none.fl_str_mv |
Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono |
| title |
Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono |
| spellingShingle |
Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono Inglidy Silva Oliveira Química inorgânica Hidróxido de magnésio Serpentina (Mineralogia) Inovações tecnológicas Termogravimetria Fluorescência de raio X Raios X – Difração Microscopia eletrônica de varredura Espectroscopia de raio X hidróxido de magnésio serpentinito aplicações tecnológicas pegada de carbono |
| title_short |
Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono |
| title_full |
Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono |
| title_fullStr |
Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono |
| title_full_unstemmed |
Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono |
| title_sort |
Transformação de serpentinito em hidróxido de magnésio para aplicações tecnológicas com menor pegada de carbono |
| author |
Inglidy Silva Oliveira |
| author_facet |
Inglidy Silva Oliveira |
| author_role |
author |
| dc.contributor.author.fl_str_mv |
Inglidy Silva Oliveira |
| dc.subject.por.fl_str_mv |
Química inorgânica Hidróxido de magnésio Serpentina (Mineralogia) Inovações tecnológicas Termogravimetria Fluorescência de raio X Raios X – Difração Microscopia eletrônica de varredura Espectroscopia de raio X |
| topic |
Química inorgânica Hidróxido de magnésio Serpentina (Mineralogia) Inovações tecnológicas Termogravimetria Fluorescência de raio X Raios X – Difração Microscopia eletrônica de varredura Espectroscopia de raio X hidróxido de magnésio serpentinito aplicações tecnológicas pegada de carbono |
| dc.subject.other.none.fl_str_mv |
hidróxido de magnésio serpentinito aplicações tecnológicas pegada de carbono |
| description |
Magnesium oxides and hydroxides have several technological applications and are important raw materials for several industrial sectors. Currently, these compounds are obtained mainly by thermal decomposition of magnesite (MgCO3), which requires high energy consumption and releases large amounts of CO2, one of the main greenhouse gases (GHGs). In this picture, an advantageous alternative is the use of serpentinite rock, which is a highly available source of non-carbonated magnesium in the world. Thus, in this work, two acidic routes were developed to obtain magnesium hydroxide from serpentinite (aqueous and thermal routes). In the aqueous route, sulfuric and hydrochloric acids were tested as leaching agents, while in the thermal route, ammonium sulfate was used. Both routes were divided into 3 main stages, characterized by the production of solids 1, 2 and 3. The influence of the parameters of temperature, reaction time and amount of leaching agent was studied considering as reference the efficiency in the extraction of magnesium from serpentinite. In the aqueous route, experiments were carried out at 3 scales – 80 mL, 1 L and 5 L, reaching a maximum magnesium extraction efficiency of 79%, with a magnesium recovery as Mg(OH)2 of 82%. Analyses by XRF showed the production of Mg(OH)2 with purities between 94-97% of MgO. In the thermal route, the efficiency in the extraction of magnesium from serpentinite was 86% and the recovery of magnesium as Mg(OH)2 was 39% with a purity of 84% of MgO, analyzed by SEM/EDS. The use of serpentinite to obtain magnesium hydroxide proved to be promising, since, from routes with low energy demand that presented satisfactory magnesium extraction efficiencies, it was possible to obtain Mg(OH)2 of high purity. |
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2025 |
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2025-02-28T19:32:59Z 2025-09-09T00:19:07Z |
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2025-02-28T19:32:59Z |
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2025-01-22 |
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Universidade Federal de Minas Gerais |
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