Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level

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In the drying process of activated clay there are two important methods that can be used to dry this activated clay: Rotator continuous drying and drying atomization. But to determine the characteristics and mechanism which intervene in the drying of clay is fundamental to use a batch tray drying. T...

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Detalles Bibliográficos
Autores: Romero y Otiniano, Pedro, Vicuña Galindo, Eder
Formato: artículo
Fecha de Publicación:2008
Institución:Universidad Nacional de Ingeniería
Repositorio:Revistas - Universidad Nacional de Ingeniería
Lenguaje:español
OAI Identifier:oai:oai:revistas.uni.edu.pe:article/362
Enlace del recurso:https://revistas.uni.edu.pe/index.php/tecnia/article/view/362
Nivel de acceso:acceso abierto
Materia:secado de bandeja
arcilla activada
bentonita activada
clay activated
bentonite activated
drying clay
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oai_identifier_str oai:oai:revistas.uni.edu.pe:article/362
network_acronym_str REVUNI
network_name_str Revistas - Universidad Nacional de Ingeniería
repository_id_str
dc.title.none.fl_str_mv Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level
Determinación de las curvas de secado mediante un secador de bandeja, en el proceso de bentonita activada con H2SO4) a nivel piloto
title Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level
spellingShingle Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level
Romero y Otiniano, Pedro
secado de bandeja
arcilla activada
bentonita activada
clay activated
bentonite activated
drying clay
title_short Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level
title_full Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level
title_fullStr Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level
title_full_unstemmed Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level
title_sort Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot level
dc.creator.none.fl_str_mv Romero y Otiniano, Pedro
Vicuña Galindo, Eder
author Romero y Otiniano, Pedro
author_facet Romero y Otiniano, Pedro
Vicuña Galindo, Eder
author_role author
author2 Vicuña Galindo, Eder
author2_role author
dc.subject.none.fl_str_mv secado de bandeja
arcilla activada
bentonita activada
clay activated
bentonite activated
drying clay
topic secado de bandeja
arcilla activada
bentonita activada
clay activated
bentonite activated
drying clay
description In the drying process of activated clay there are two important methods that can be used to dry this activated clay: Rotator continuous drying and drying atomization. But to determine the characteristics and mechanism which intervene in the drying of clay is fundamental to use a batch tray drying. The objective of the present work is obtain the curve of drying velocity, fixing sorne initial conditions of humidity, and to define the mechanisms involved in the drying of activated clay with sulphuric acid. Further, this information will be used to scale to continuous drying and find out the equations which govern this process. It was necessary to use a tray of 214 cm2 surface area to charge moist bentonite. Samples were taken containing between 48 and 138 g, and initial humidity between 38 and 50%; to achieve a.final humidity of between about 8 and 13%. Graph of clay total mass (MT) versus drying time (0) show two periods: firstly a linear trend, followed by a no-linear trend. This second period consist of two stages, the first one consist in the formation of a rigid structure ar semi-rigid on the surface of the so/id. The second one consists in the removal of the moisture balance and this is frequently accompanied by an internal vaporization which can cause the so/id expansion. These drying characteristics are presented in graphic N°6 as a curve of drying velocity vs. solid humidity. These second period can be represented by the equation: Wc= 0.003463Xm^1.6556 .
publishDate 2008
dc.date.none.fl_str_mv 2008-06-01
dc.type.none.fl_str_mv info:eu-repo/semantics/article
info:eu-repo/semantics/publishedVersion
Artículo evaluado por pares
format article
status_str publishedVersion
dc.identifier.none.fl_str_mv https://revistas.uni.edu.pe/index.php/tecnia/article/view/362
10.21754/tecnia.v18i1.362
url https://revistas.uni.edu.pe/index.php/tecnia/article/view/362
identifier_str_mv 10.21754/tecnia.v18i1.362
dc.language.none.fl_str_mv spa
language spa
dc.relation.none.fl_str_mv https://revistas.uni.edu.pe/index.php/tecnia/article/view/362/356
dc.rights.none.fl_str_mv Derechos de autor 2008 TECNIA
http://creativecommons.org/licenses/by/4.0
info:eu-repo/semantics/openAccess
rights_invalid_str_mv Derechos de autor 2008 TECNIA
http://creativecommons.org/licenses/by/4.0
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv Universidad Nacional de Ingeniería
publisher.none.fl_str_mv Universidad Nacional de Ingeniería
dc.source.none.fl_str_mv TECNIA; Vol. 18 No. 1 (2008); 49-59
TECNIA; Vol. 18 Núm. 1 (2008); 49-59
2309-0413
0375-7765
reponame:Revistas - Universidad Nacional de Ingeniería
instname:Universidad Nacional de Ingeniería
instacron:UNI
instname_str Universidad Nacional de Ingeniería
instacron_str UNI
institution UNI
reponame_str Revistas - Universidad Nacional de Ingeniería
collection Revistas - Universidad Nacional de Ingeniería
repository.name.fl_str_mv
repository.mail.fl_str_mv
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spelling Determination of the drying curves by means of a tray dryer, in the bentonite process activated with H2SO4) at a pilot levelDeterminación de las curvas de secado mediante un secador de bandeja, en el proceso de bentonita activada con H2SO4) a nivel pilotoRomero y Otiniano, PedroVicuña Galindo, Edersecado de bandejaarcilla activadabentonita activadaclay activatedbentonite activateddrying clayIn the drying process of activated clay there are two important methods that can be used to dry this activated clay: Rotator continuous drying and drying atomization. But to determine the characteristics and mechanism which intervene in the drying of clay is fundamental to use a batch tray drying. The objective of the present work is obtain the curve of drying velocity, fixing sorne initial conditions of humidity, and to define the mechanisms involved in the drying of activated clay with sulphuric acid. Further, this information will be used to scale to continuous drying and find out the equations which govern this process. It was necessary to use a tray of 214 cm2 surface area to charge moist bentonite. Samples were taken containing between 48 and 138 g, and initial humidity between 38 and 50%; to achieve a.final humidity of between about 8 and 13%. Graph of clay total mass (MT) versus drying time (0) show two periods: firstly a linear trend, followed by a no-linear trend. This second period consist of two stages, the first one consist in the formation of a rigid structure ar semi-rigid on the surface of the so/id. The second one consists in the removal of the moisture balance and this is frequently accompanied by an internal vaporization which can cause the so/id expansion. These drying characteristics are presented in graphic N°6 as a curve of drying velocity vs. solid humidity. These second period can be represented by the equation: Wc= 0.003463Xm^1.6556 .En el proceso de secado de la arcilla activada, existen dos métodos importantes que se pueden usar para secar arcillas activadas: Secador Rotatorio Continuo [l] y Secador por Atomización (6). Pero para determinar las características y mecanismos que intervienen en el secado de la arcilla es fundamental utilizar un secador de bandeja por lote. El objetivo del presente trabajo es obtener la curva de velocidad de secado, fijando ciertas condiciones iniciales de humedad, y definir los mecanismos que intervienen en el secado de las arcillas activadas con ácido sulfúrico, permitiendo utilizar esta información en los procesos de secado continuo, así como encontrar las ecuaciones que gobiernan los diferentes mecanismos de secado. Se utilizó una bandeja de área superficial de 214 cm2 en la cual se carga la bentonita húmeda, las muestras tomadas fueron de 48 a 138 g aprox. y 38 a 50% de humedad inicial para llevarla a una humedad final de 8 a 13%. Se representó la Masa Total de Arcilla (MT) vs. Tiempo de Secado (O), mostrándose dos periodos, uno de tendencia lineal, presentándose luego una desviación, este segundo periodo consta de dos etapas, la primera etapa consiste en la formación de una estructura rígida o semirrígida en la superficie del sólido, la segunda es la remoción de la humedad remanente y esto esta frecuentemente acompañado por una vaporización interna, la cual puede causar la expansión del sólido. Estas características de secado están representadas en la Fig. 6, como una curva de velocidad de secado vs. humedad del sólido. Este segundo período puede ser representado por la ecuación: Wc= 0.003463Xm^1.6556 .Universidad Nacional de Ingeniería2008-06-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionArtículo evaluado por paresapplication/pdfhttps://revistas.uni.edu.pe/index.php/tecnia/article/view/36210.21754/tecnia.v18i1.362TECNIA; Vol. 18 No. 1 (2008); 49-59TECNIA; Vol. 18 Núm. 1 (2008); 49-592309-04130375-7765reponame:Revistas - Universidad Nacional de Ingenieríainstname:Universidad Nacional de Ingenieríainstacron:UNIspahttps://revistas.uni.edu.pe/index.php/tecnia/article/view/362/356Derechos de autor 2008 TECNIAhttp://creativecommons.org/licenses/by/4.0info:eu-repo/semantics/openAccessoai:oai:revistas.uni.edu.pe:article/3622023-12-05T16:59:00Z
score 13.785607
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