Campo DC | Valor | Idioma |
dc.creator | Souza, Ana Carolina Santos de | - |
dc.date.accessioned | 2024-01-12T15:33:17Z | - |
dc.date.available | 2024-01-12T15:33:17Z | - |
dc.date.issued | 2023-10-10 | - |
dc.identifier.uri | https://repositorio.ufba.br/handle/ri/38864 | - |
dc.description.abstract | Monazite is one of the primary light rare earth minerals and it is always associated with the
presence of thorium. This poses challenges in processing due to the strong radiation present in
this mineral. This study addresses the separation of thorium from light rare earth elements in
hydrochloric acid medium from desphosphorized monazite. The steps used to obtain an aqueous
solution involved: addition of NaOH to the concentrate, heating at a temperature of 400°C for
3 hours, washing with water, and subsequent leaching of the residue with HCl. Samples from
the aqueous phase were analyzed by ICP-OES. To assess the feasibility of alkaline fusion,
thermodynamic modeling with different reagents was performed, and thermodynamic
calculations of probable reactions were conducted using the HSC Chemistry 6.0 software
database. NaOH appears as the most effective reagent from a thermodynamic and energetic
standpoint. The separation of thorium from light rare earth elements was carried out through
solvent extraction using compounds such as Cyanex 572, 272, 923, 921, and mixtures.
Theoretical modeling was conducted using the Spana software to compare conditions in nitric
and hydrochloric media. It was observed that Cyanex 572 and its mixtures extract 98% of the
thorium in ane single stage, while Cyanex 272 extracts 70% of the thorium and 40% of the
LREEs. The results show that thorium can be separated from light rare earth elements in
hydrochloric medium, both by Cyanex 272 and Cyanex 572, requiring an additional extraction
stage when using Cyanex 272. The other extractants did not yield satisfactory results in the
separation. The results indicate that extraction capacity can be improved by using long-chain
diluents, an acidic pH below 2, and a concentration of 5% for Cyanex 572 and 10% for Cyanex
272. | pt_BR |
dc.language | por | pt_BR |
dc.publisher | UNIVERSIDADE FEDERAL DA BAHIA | pt_BR |
dc.subject | Monazita | pt_BR |
dc.subject | Fusão alcalina | pt_BR |
dc.subject | Termodinâmica | pt_BR |
dc.subject | Elementos terras raras | pt_BR |
dc.subject | Separação do tório | pt_BR |
dc.subject | Extração por solvente | pt_BR |
dc.subject.other | Monazite | pt_BR |
dc.subject.other | Alkaline fusion | pt_BR |
dc.subject.other | thermodynamics | pt_BR |
dc.subject.other | Rare earth elements | pt_BR |
dc.subject.other | Thorium separation | pt_BR |
dc.subject.other | Solvent extraction | pt_BR |
dc.title | Decomposição térmica de monazita e separação do tório dos elementos terras raras leves em meio clorídríco, pela técnica de extração por solvente | pt_BR |
dc.type | Tese | pt_BR |
dc.publisher.program | Programa de Pós-Graduação em Engenharia Industrial (PEI) | pt_BR |
dc.publisher.initials | UFBA | pt_BR |
dc.publisher.country | Brasil | pt_BR |
dc.subject.cnpq | CNPQ::ENGENHARIAS | pt_BR |
dc.contributor.advisor1 | Lima, Luiz Rogério Pinho de Andrade | - |
dc.contributor.advisor1Lattes | https://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4785397A2&tokenCaptchar=03AFcWeA7yHOzPs31axqfVNT-jkjf4irX-0hMIJwG00K-r2TglcBx448Ivk4_tEpLG3ABB3q6kSGkqeN15lH-hzQLSzFc8TDGQ6h30KzgaDPWBEug_UHBxTF2v1-2rV4o6SCZlmbi1vKyWa0eshBohJ3hiSR9g6eC8Ap56HkgaTwep1dgdDmqbRD12BF6Hj6htIx5KPak5iHoCzP064iNh7opvxEYx1gxvotfr-dQA9EKYuzRmKAUQ6m_3XW6eNiEGurROEUCXz8u23QSHNFJYvvbUN9-gOrTQCgrgX2MZsQVOAJ30QfgqEwp4XfysJpc-tiAlcysjzxsuNk9hzEM-uV2bLzsas8LncK0Y3sO4qg83joP6X5XI1bHVcXQkbzMh5dr8TRd1BK_HuHgbjcSTEX0zo7KPT8W-y9PDDK-LKKOdGOCd5B4ux-HujghYJl-jH4d8AMTBPIsLtarf0w14mkX7MfqwNZ1QyCELNCV1wJm9GFIZRVRjDxlKvU205uzuyOC1ITCMjZfsOi3A1C9igH6rvva_vzHq6GWMhxjQhyDEJrhwPbyYoG4Z5qfllxoAN34gsrfyYq_1xvxBKulXc_NnOTSFo664rXX102LaV6vltMsoK1IgbYxew2efROrPByaYtPI6ZUeTp4mCQFTY59XopzNlAxAqOg | pt_BR |
dc.contributor.referee1 | Morais, Carlos Antônio | - |
dc.contributor.referee1Lattes | https://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4761196Z6&tokenCaptchar=03AFcWeA6yqZQhTK3i5163ZYz_po-HVr4q2ci_-LqF-TschkWPhaa5dqoj5UVRvBN5-UPUgT9ptNUn4IRz7OhlFFpRkokASiMaaqgkXB-zINviFp90ngtvfo7FEUVkwBhT09mqV28fhxLCzolleOnBp-FLbhwye_4T1qlxFAMJHum1ha6RGucUCPqSntiJzPCU1LJ2zQobWgzVSQogI-dXuKhs_q_LEqh2eFtlHJkHJRlAXQxCPN_eRZp_8-X-V6f0Aei1ivW2y0PXi9G0Y9XMRGQCuSqICRRbLck9ILFTaTKblBeVXMBfnHxTon695EVBZsz9q6TGZaMTsM_0D_EqYHKm0AY6Fbrl1fx7-GxGB3K10htNv8MAwP9oovFBMXZ6cOGbR8ils6tZOZ2E324MHpbMF0OFotraC5GoOtnT9CpWydkEID_5TLvo5Kb3Cwerb4_JoCctmQP8AxKIJph1pMbIuw3BLCRr7hHH2OYuWLCLfoODyunOu3eQ2RERzaIzqjKztlDxBcLUpRpqyNeg7LCoXitwvVZAwNHisdPm3Wa6uhXg1j1GLrc3J7Y7jEAsIpUSI4M9QAajfqlVwve2OjAtxYelkcfaaGlIptodNFyODygxupoFBBx-5cvPxpglQ37EMIpyrO_fb_pRpirtFec7g3ZZT3tKNg | pt_BR |
dc.contributor.referee2 | Leão, Versiane Albis | - |
dc.contributor.referee2Lattes | https://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4728971Z4&tokenCaptchar=03AFcWeA69vgc9y4j4Mq1qKo3fIT16ebGjp_DZ-x03QZShelmRHKK1a2jM5H78wrqRjxD7d5cFZ3UAMZhj4SGkjGY76odbyeWQyD572c3fuUrS107ojA8mgYvILJoVIwBWwMUS9MD1cWAmlhkeVkyk39hyLIqb90SNb-ec6Tg13T_0zGkMkqLLvbrgvTk8bsMr6doV9RyJuw8AcwZdQj4tdeTm_WCTJpB8bTysMylNh2Akw9CdFdd26ILAnmcd4hn4Dgr1Y5b_sDq9pZIuR4tCKDSTrRZeaydPolwwvHjfsaR4GvSKFlJu_RheZ6xca5YLSE9dDY53xtRImEAZmmmloSWk2J7ZYU02w_UZvR14YLZ8cxaMkbjir8CikrAArhzD7t1K2kGEmbDkoApQlKeiVaiDEdglHM2uXIKw2JLxJqYDaoExoSWsO-84Kr0iNANfY6QjylZUTxp8e66T05FcDnwDWpZJFp2GIRp7-zMw3OBnpWaPACVEooN6WHtxADwUF-qyIqDweluOjEXyBaYjPISp3Y-nxpJTNKGnAk8n7z6Q3WkeG_kiYJce_yPoxS2_XTrm3PvSYUfVJAS-duccFZlrmRJ3fwDj7muxBZk5JECCg65a5z-C9K3kIw8pqQ6T875_CHv98JvGqGj2m8blHotb_YHTTVZAJg | pt_BR |
dc.contributor.referee3 | Mansur, Marcelo Borges | - |
dc.contributor.referee3Lattes | https://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4760351Z2&tokenCaptchar=03AFcWeA7e-uENRtQBAYi1CaIy87N9RSYK5cZHP5HTstMN07be_sBIHjIzwKasw_7yZCISOdi5X9YOgKpqtTwvTBQ1Bi-YKgCguDO7RAanaibFELrDOvNkqEAu10eVp1OLmoxETaOy1c8yM6z9ZvFRyjaWmbNlk2fxYGtVL_4oGCnhKcIumkLNGnkVo2Fhr5E368dPqAyQZ7isyCcRD7upT23JOjZqYqsc88AdW56BoGv6-4wNLA0k-UrL88hek0VPIN-yatrVZC085iX6qkCHgRieguL3sVdbYohx7wafqNzQ3PPansht2v1sC031GpL5VD2QPOwww2MdOjym6FHibpm8DU0-LA_sqKIhorDXbizUxSKTexevxy9r0grMOqqiy2jCNu5Rnx5r7OdFcN82a1Dy0OTGlKhO4NkX6WI6ipz7T810EnOHAUheLPiO4TmPco4O2vr1Mf1YY5rUobSr5L8gPmB_WE5kWP-6JATOuNu8bXff6IjcxDOISdROLWk95Guf-2Hgeqb6jIxTx0f4nrB5-OpoFmG4h2t0J4CGv7B5Bq3ltbLd-GZ3IllYe0cCkbzVK5k3-kgXFhqSKbb4JfDK2gfmUjIqy56UwuGDrnv9HhdZlhoqzAZePQxUxyYa-1xQcqgOs1wvpvRXtkh__aWiOXInpyLe2w | pt_BR |
dc.contributor.referee4 | Silva, André Carlos | - |
dc.contributor.referee4Lattes | https://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4762595Z9&tokenCaptchar=03AFcWeA57wDiFuhx3cAzunAe_YIQstAAMcWgPm_ffSOc1GuF92bfteJvc1-M0CWVf6bjPH33P2f4HqbQd8eoWxuiz8Z3ZexMGEvyivVMa_A7eT9JkNIaEb1mQMX6zbin3UY5QOkR_dGSUa7-49shg9DgAEuPW4rMNlmr1wHACf0CX_aWC4ElZGGpaGYsuV8pPjHG_KO2aq7MI6YMNekmsPsPcvPCGhFIky23--S71bYzQh-hjIeDGf9elpe2YjNIFBfjNOWUQY6dkzAEBiiCKqKiCa_c9jYsB9_F5XtOHNuIO1SMSd9ewVwa8NEZRDE-ru80FAEob3aMd18n1-2MgPxVieN1ozsgxyBFSgJ_RlGOcYQXSJlV4-YzIZxAnTu6p7OG2M0Edazg7cJBp62sP5VT_jcb1Hr91_tp4jEYy6Lk0bFTBXqP_epNLDaByDStQIHHAnF8IsNkXfVXoTDaZbPeF9Omug1Lz8SeH7iav5Ed7p6kTAl-4iLeDEH0HvBZyShfJWf84ecwRHVwgnJDOqa2Kc8mJOQ6Pa18Obq0Gn_5lhWZJdlaXH23OHYrc8ApVIRkJTRTJBCv6VWQ6_-oZ3GBOsx5yXPRq6qKpip75jUUF0JaXQaG-H5LOG2kCFl1CJ1iuS7hwoo7zKzzQh_iEUYyehJ6pW9q7Ag | pt_BR |
dc.contributor.referee5 | Lima, Luiz Rogério Pinho de Andrade | - |
dc.contributor.referee5Lattes | https://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4785397A2&tokenCaptchar=03AFcWeA7yHOzPs31axqfVNT-jkjf4irX-0hMIJwG00K-r2TglcBx448Ivk4_tEpLG3ABB3q6kSGkqeN15lH-hzQLSzFc8TDGQ6h30KzgaDPWBEug_UHBxTF2v1-2rV4o6SCZlmbi1vKyWa0eshBohJ3hiSR9g6eC8Ap56HkgaTwep1dgdDmqbRD12BF6Hj6htIx5KPak5iHoCzP064iNh7opvxEYx1gxvotfr-dQA9EKYuzRmKAUQ6m_3XW6eNiEGurROEUCXz8u23QSHNFJYvvbUN9-gOrTQCgrgX2MZsQVOAJ30QfgqEwp4XfysJpc-tiAlcysjzxsuNk9hzEM-uV2bLzsas8LncK0Y3sO4qg83joP6X5XI1bHVcXQkbzMh5dr8TRd1BK_HuHgbjcSTEX0zo7KPT8W-y9PDDK-LKKOdGOCd5B4ux-HujghYJl-jH4d8AMTBPIsLtarf0w14mkX7MfqwNZ1QyCELNCV1wJm9GFIZRVRjDxlKvU205uzuyOC1ITCMjZfsOi3A1C9igH6rvva_vzHq6GWMhxjQhyDEJrhwPbyYoG4Z5qfllxoAN34gsrfyYq_1xvxBKulXc_NnOTSFo664rXX102LaV6vltMsoK1IgbYxew2efROrPByaYtPI6ZUeTp4mCQFTY59XopzNlAxAqOg | pt_BR |
dc.creator.Lattes | https://buscatextual.cnpq.br/buscatextual/visualizacv.do?id=K4334930H6&tokenCaptchar=03AFcWeA5F0-F7VhvuJWxltrQ42o13xc9WNRHeoPUGkZYTglnOe84HsULC8TfTwXgx2ROHbcc9vDjp119zaWl58_5kkC3l4OTQK_l5llXq_zEO6jXWgG4mbqSBi5C6IicPr2uj6kth9gbfzRsFje6JhTR8Mb5RPw9uBu4CG-FqrzEOOpzmdjumjksqvF5WYeQY4CuEZUh4REqxX3jKu08V2GJRW_eNNlIz1FLwOgTBHqNDS64vSquDUTKEof83yma7aWUrA_J6Jbgc3NyBc4iLzH6nvoU2vkhuAm_zvEDnaK3n9RejOjkQRWrw920wAALNh-5ar427IrKD3_AV007tJyZ48s1Py01z3lVzjef3VU4pUf5bp-NKWS9AXQO20eeve0QafdigzC2LCXq8JHciWG8g9wWxlw_XK5Jy653_fFx0YiCWqlAeO53GfVfCp-KfN43i2Tg5LXDBcUPKgwXJHTCMlojBnNA3K97nsVHxQ2htlMfTmWsaERkcHW7zv8hcH9_7TpwEMTNW5LzK7NYDKArZuxLRzfGWnOXQkUrn8UgI-m8Z0oay4-AHfGqsywMqXeZR5ZKtP5SlqHGJBUUE2SA3Pcue0Dcg4gJKkvjbuw-d5-2AWWyqIXtZelqVnwFV1ekE6YUE_8baSkoAB7dV0jLIGL7bC-r-sA | pt_BR |
dc.description.resumo | Monazita é um dos principais minerais de terras raras leves e está sempre associada à presença de
tório. Isso representa desafios no processamento devido à forte radiação presente neste mineral.
Neste estudo, é abordada a separação do tório dos elementos terras raras leves em meio clorídrico
a partir de monazita desfosforada. As etapas usadas para obter uma solução aquosa envolveram:
adição de NaOH ao concentrado, aquecimento à temperatura de 400 oC por 3 horas, lavagem com
água e posterior lixiviação do resíduo com HCl. As amostras da fase aquosa foram analisadas por
ICP-OES. Para verificar a viabilidade da fusão alcalina, uma modelagem termodinâmica com
diferentes reagentes foi realizada, e os cálculos termodinâmicos das prováveis reações foram feitos
consultando o banco de dados do software HSC Chemistry 6.0. O NaOH se apresenta como o
reagente mais eficaz do ponto de vista termodinâmico e energético. A separação do tório dos
elementos de terras raras leves foi realizada por extração com solventes como Cyanex 572, 272,
923, 921 e misturas. Foi realizada uma modelagem teórica utilizando o software Spana para
comparar as condições nos meios nítrico e clorídrico. Observou-se que o Cyanex 572 e suas
misturas extraem 98% do tório em um único estágio, enquanto Cyanex 272 extrai 70% do tório e
40% dos ETR. Os resultados mostram que o tório pode ser separado dos ETR leves em meio
clorídrico, tanto por Cyanex 272 quanto por Cyanex 572, sendo necessário um estágio adicional de
extração ao utilizar o Cyanex 272. Os demais extratantes não apresentaram resultados satisfatórios
na separação. Os resultados mostram que a capacidade de extração pode ser melhorada utilizando
diluentes de cadeia longa, pH ácido, abaixo de 2 e concentração de 5% para o Cyanex 572 e 10%
para o Cyanex 272. | pt_BR |
dc.publisher.department | Escola Politécnica | pt_BR |
dc.type.degree | Doutorado | pt_BR |
Aparece nas coleções: | Tese (PEI)
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