Influence of the evaporation rate over lithium recovery from brines
- Autores
- Valdez, Silvana Karina; Flores, Horacio Ricardo; Orce, Agustina
- Año de publicación
- 2016
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- The brines of the South American Puna contain a great amount of valuables ions. Among them, lithium has the highest economic value; therefore, its grade and recovery are of interest in the purification steps of the brine. The first step of the process is brine concentration by solar evaporation. This process involves the precipitation of the ions which form saturated brines and a mass of crystals impregnated with mother liquor is obtained. The first salt that precipitates is sodium chloride (NaCl) because of their high initial concentration. When approximately 60% of the water is evaporated, a mixture of NaCl and KCl (sylvite) is obtained. This by product is used as raw material to obtain potassium chloride (KCl). The others ions present in the brine such as magnesium, calcium, and sulphate precipitate by adding a specific reagent (chemical precipitation). Sulphate and calcium precipitate as CaSO4, and magnesium as Mg(OH)2. The purified solution is sent to a final evaporation stage where the concentration of Li+ increases to about 6%.At each evaporation step, the ionic concentrations of the brine increases. In contrast its volume decreases. Also, the crystals obtained are soaked with a brine which is increasingly concentrated in lithium. Thus, the limiting factor to a greater degree of evaporation is the loss of Li+with the rich solution accompanying the mass of crystals. This liquor is the limiting factor in the evaporation level when a higher lithium grade is required. In this paper a progressive evaporation of brines from the North West of Argentina was performed and analyzed, focused in the lithium recovery from the concentrated brine. For a given brine, it is shown thatwhen the 64.3% of evaporation in volume is reached, the lithium concentration increases from 900 to 7,200 ppm. In this case, it is obtained a brine yield of 33.5 % in volume and a lithium recovery of the 28.1%.On the other hand, when the evaporation reaches 40% in volume, lithium recovery is 74%.
Fil: Valdez, Silvana Karina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones para la Industria Química; Argentina
Fil: Flores, Horacio Ricardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones para la Industria Química; Argentina
Fil: Orce, Agustina. Universidad Nacional de Salta. Facultad de Ingenieria; Argentina - Materia
-
BRINES
EVAPORATION RATE
LITHIUM
RECOVERY - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
- Repositorio
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/62699
Ver los metadatos del registro completo
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Influence of the evaporation rate over lithium recovery from brinesValdez, Silvana KarinaFlores, Horacio RicardoOrce, AgustinaBRINESEVAPORATION RATELITHIUMRECOVERYhttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2The brines of the South American Puna contain a great amount of valuables ions. Among them, lithium has the highest economic value; therefore, its grade and recovery are of interest in the purification steps of the brine. The first step of the process is brine concentration by solar evaporation. This process involves the precipitation of the ions which form saturated brines and a mass of crystals impregnated with mother liquor is obtained. The first salt that precipitates is sodium chloride (NaCl) because of their high initial concentration. When approximately 60% of the water is evaporated, a mixture of NaCl and KCl (sylvite) is obtained. This by product is used as raw material to obtain potassium chloride (KCl). The others ions present in the brine such as magnesium, calcium, and sulphate precipitate by adding a specific reagent (chemical precipitation). Sulphate and calcium precipitate as CaSO4, and magnesium as Mg(OH)2. The purified solution is sent to a final evaporation stage where the concentration of Li+ increases to about 6%.At each evaporation step, the ionic concentrations of the brine increases. In contrast its volume decreases. Also, the crystals obtained are soaked with a brine which is increasingly concentrated in lithium. Thus, the limiting factor to a greater degree of evaporation is the loss of Li+with the rich solution accompanying the mass of crystals. This liquor is the limiting factor in the evaporation level when a higher lithium grade is required. In this paper a progressive evaporation of brines from the North West of Argentina was performed and analyzed, focused in the lithium recovery from the concentrated brine. For a given brine, it is shown thatwhen the 64.3% of evaporation in volume is reached, the lithium concentration increases from 900 to 7,200 ppm. In this case, it is obtained a brine yield of 33.5 % in volume and a lithium recovery of the 28.1%.On the other hand, when the evaporation reaches 40% in volume, lithium recovery is 74%.Fil: Valdez, Silvana Karina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones para la Industria Química; ArgentinaFil: Flores, Horacio Ricardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones para la Industria Química; ArgentinaFil: Orce, Agustina. Universidad Nacional de Salta. Facultad de Ingenieria; ArgentinaWJRR2016-07info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/62699Valdez, Silvana Karina; Flores, Horacio Ricardo; Orce, Agustina; Influence of the evaporation rate over lithium recovery from brines; WJRR; World Journal of Research and Review (WJRR); 3; 1; 7-2016; 66-702455-3956CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/https://www.wjrr.org/download_data/WJRR0301093.pdfinfo:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-29T09:44:10Zoai:ri.conicet.gov.ar:11336/62699instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-09-29 09:44:11.183CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
Influence of the evaporation rate over lithium recovery from brines |
title |
Influence of the evaporation rate over lithium recovery from brines |
spellingShingle |
Influence of the evaporation rate over lithium recovery from brines Valdez, Silvana Karina BRINES EVAPORATION RATE LITHIUM RECOVERY |
title_short |
Influence of the evaporation rate over lithium recovery from brines |
title_full |
Influence of the evaporation rate over lithium recovery from brines |
title_fullStr |
Influence of the evaporation rate over lithium recovery from brines |
title_full_unstemmed |
Influence of the evaporation rate over lithium recovery from brines |
title_sort |
Influence of the evaporation rate over lithium recovery from brines |
dc.creator.none.fl_str_mv |
Valdez, Silvana Karina Flores, Horacio Ricardo Orce, Agustina |
author |
Valdez, Silvana Karina |
author_facet |
Valdez, Silvana Karina Flores, Horacio Ricardo Orce, Agustina |
author_role |
author |
author2 |
Flores, Horacio Ricardo Orce, Agustina |
author2_role |
author author |
dc.subject.none.fl_str_mv |
BRINES EVAPORATION RATE LITHIUM RECOVERY |
topic |
BRINES EVAPORATION RATE LITHIUM RECOVERY |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
The brines of the South American Puna contain a great amount of valuables ions. Among them, lithium has the highest economic value; therefore, its grade and recovery are of interest in the purification steps of the brine. The first step of the process is brine concentration by solar evaporation. This process involves the precipitation of the ions which form saturated brines and a mass of crystals impregnated with mother liquor is obtained. The first salt that precipitates is sodium chloride (NaCl) because of their high initial concentration. When approximately 60% of the water is evaporated, a mixture of NaCl and KCl (sylvite) is obtained. This by product is used as raw material to obtain potassium chloride (KCl). The others ions present in the brine such as magnesium, calcium, and sulphate precipitate by adding a specific reagent (chemical precipitation). Sulphate and calcium precipitate as CaSO4, and magnesium as Mg(OH)2. The purified solution is sent to a final evaporation stage where the concentration of Li+ increases to about 6%.At each evaporation step, the ionic concentrations of the brine increases. In contrast its volume decreases. Also, the crystals obtained are soaked with a brine which is increasingly concentrated in lithium. Thus, the limiting factor to a greater degree of evaporation is the loss of Li+with the rich solution accompanying the mass of crystals. This liquor is the limiting factor in the evaporation level when a higher lithium grade is required. In this paper a progressive evaporation of brines from the North West of Argentina was performed and analyzed, focused in the lithium recovery from the concentrated brine. For a given brine, it is shown thatwhen the 64.3% of evaporation in volume is reached, the lithium concentration increases from 900 to 7,200 ppm. In this case, it is obtained a brine yield of 33.5 % in volume and a lithium recovery of the 28.1%.On the other hand, when the evaporation reaches 40% in volume, lithium recovery is 74%. Fil: Valdez, Silvana Karina. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones para la Industria Química; Argentina Fil: Flores, Horacio Ricardo. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Salta. Instituto de Investigaciones para la Industria Química. Universidad Nacional de Salta. Facultad de Ingeniería. Instituto de Investigaciones para la Industria Química; Argentina Fil: Orce, Agustina. Universidad Nacional de Salta. Facultad de Ingenieria; Argentina |
description |
The brines of the South American Puna contain a great amount of valuables ions. Among them, lithium has the highest economic value; therefore, its grade and recovery are of interest in the purification steps of the brine. The first step of the process is brine concentration by solar evaporation. This process involves the precipitation of the ions which form saturated brines and a mass of crystals impregnated with mother liquor is obtained. The first salt that precipitates is sodium chloride (NaCl) because of their high initial concentration. When approximately 60% of the water is evaporated, a mixture of NaCl and KCl (sylvite) is obtained. This by product is used as raw material to obtain potassium chloride (KCl). The others ions present in the brine such as magnesium, calcium, and sulphate precipitate by adding a specific reagent (chemical precipitation). Sulphate and calcium precipitate as CaSO4, and magnesium as Mg(OH)2. The purified solution is sent to a final evaporation stage where the concentration of Li+ increases to about 6%.At each evaporation step, the ionic concentrations of the brine increases. In contrast its volume decreases. Also, the crystals obtained are soaked with a brine which is increasingly concentrated in lithium. Thus, the limiting factor to a greater degree of evaporation is the loss of Li+with the rich solution accompanying the mass of crystals. This liquor is the limiting factor in the evaporation level when a higher lithium grade is required. In this paper a progressive evaporation of brines from the North West of Argentina was performed and analyzed, focused in the lithium recovery from the concentrated brine. For a given brine, it is shown thatwhen the 64.3% of evaporation in volume is reached, the lithium concentration increases from 900 to 7,200 ppm. In this case, it is obtained a brine yield of 33.5 % in volume and a lithium recovery of the 28.1%.On the other hand, when the evaporation reaches 40% in volume, lithium recovery is 74%. |
publishDate |
2016 |
dc.date.none.fl_str_mv |
2016-07 |
dc.type.none.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
format |
article |
status_str |
publishedVersion |
dc.identifier.none.fl_str_mv |
http://hdl.handle.net/11336/62699 Valdez, Silvana Karina; Flores, Horacio Ricardo; Orce, Agustina; Influence of the evaporation rate over lithium recovery from brines; WJRR; World Journal of Research and Review (WJRR); 3; 1; 7-2016; 66-70 2455-3956 CONICET Digital CONICET |
url |
http://hdl.handle.net/11336/62699 |
identifier_str_mv |
Valdez, Silvana Karina; Flores, Horacio Ricardo; Orce, Agustina; Influence of the evaporation rate over lithium recovery from brines; WJRR; World Journal of Research and Review (WJRR); 3; 1; 7-2016; 66-70 2455-3956 CONICET Digital CONICET |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
info:eu-repo/semantics/altIdentifier/url/https://www.wjrr.org/download_data/WJRR0301093.pdf |
dc.rights.none.fl_str_mv |
info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
eu_rights_str_mv |
openAccess |
rights_invalid_str_mv |
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
dc.format.none.fl_str_mv |
application/pdf application/pdf application/pdf |
dc.publisher.none.fl_str_mv |
WJRR |
publisher.none.fl_str_mv |
WJRR |
dc.source.none.fl_str_mv |
reponame:CONICET Digital (CONICET) instname:Consejo Nacional de Investigaciones Científicas y Técnicas |
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CONICET Digital (CONICET) |
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CONICET Digital (CONICET) |
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Consejo Nacional de Investigaciones Científicas y Técnicas |
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CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas |
repository.mail.fl_str_mv |
dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar |
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13.070432 |