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
CONICET Digital (CONICET)
Institución
Consejo Nacional de Investigaciones Científicas y Técnicas
OAI Identificador
oai:ri.conicet.gov.ar:11336/62699

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spelling 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
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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
reponame_str CONICET Digital (CONICET)
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instname_str Consejo Nacional de Investigaciones Científicas y Técnicas
repository.name.fl_str_mv 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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