Modeling and simulation of direct contact evaporators

Bibliographic Details
Main Author: Campos,F.B.
Publication Date: 2001
Other Authors: Lage,P.L.C.
Format: Article
Language: eng
Source: Brazilian Journal of Chemical Engineering
Download full: http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322001000300007
Summary: A dynamic model of a direct contact evaporator was developed and coupled to a recently developed superheated bubble model. The latter model takes into account heat and mass transfer during the bubble formation and ascension stages and is able to predict gas holdup in nonisothermal systems. The results of the coupled model, which does not have any adjustable parameter, were compared with experimental data. The transient behavior of the liquid-phase temperature and the vaporization rate under quasi-steady-state conditions were in very good agreement with experimental data. The transient behavior of liquid height was only reasonably simulated. In order to explain this partial disagreement, some possible causes were analyzed.
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spelling Modeling and simulation of direct contact evaporatorsheat and mass transferdirect contact evaporatormodeling and simulationbubblebubble columnA dynamic model of a direct contact evaporator was developed and coupled to a recently developed superheated bubble model. The latter model takes into account heat and mass transfer during the bubble formation and ascension stages and is able to predict gas holdup in nonisothermal systems. The results of the coupled model, which does not have any adjustable parameter, were compared with experimental data. The transient behavior of the liquid-phase temperature and the vaporization rate under quasi-steady-state conditions were in very good agreement with experimental data. The transient behavior of liquid height was only reasonably simulated. In order to explain this partial disagreement, some possible causes were analyzed.Brazilian Society of Chemical Engineering2001-09-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322001000300007Brazilian Journal of Chemical Engineering v.18 n.3 2001reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322001000300007info:eu-repo/semantics/openAccessCampos,F.B.Lage,P.L.C.eng2001-10-10T00:00:00Zoai:scielo:S0104-66322001000300007Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2001-10-10T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false
dc.title.none.fl_str_mv Modeling and simulation of direct contact evaporators
title Modeling and simulation of direct contact evaporators
spellingShingle Modeling and simulation of direct contact evaporators
Campos,F.B.
heat and mass transfer
direct contact evaporator
modeling and simulation
bubble
bubble column
title_short Modeling and simulation of direct contact evaporators
title_full Modeling and simulation of direct contact evaporators
title_fullStr Modeling and simulation of direct contact evaporators
title_full_unstemmed Modeling and simulation of direct contact evaporators
title_sort Modeling and simulation of direct contact evaporators
author Campos,F.B.
author_facet Campos,F.B.
Lage,P.L.C.
author_role author
author2 Lage,P.L.C.
author2_role author
dc.contributor.author.fl_str_mv Campos,F.B.
Lage,P.L.C.
dc.subject.por.fl_str_mv heat and mass transfer
direct contact evaporator
modeling and simulation
bubble
bubble column
topic heat and mass transfer
direct contact evaporator
modeling and simulation
bubble
bubble column
description A dynamic model of a direct contact evaporator was developed and coupled to a recently developed superheated bubble model. The latter model takes into account heat and mass transfer during the bubble formation and ascension stages and is able to predict gas holdup in nonisothermal systems. The results of the coupled model, which does not have any adjustable parameter, were compared with experimental data. The transient behavior of the liquid-phase temperature and the vaporization rate under quasi-steady-state conditions were in very good agreement with experimental data. The transient behavior of liquid height was only reasonably simulated. In order to explain this partial disagreement, some possible causes were analyzed.
publishDate 2001
dc.date.none.fl_str_mv 2001-09-01
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322001000300007
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322001000300007
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/S0104-66322001000300007
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv text/html
dc.publisher.none.fl_str_mv Brazilian Society of Chemical Engineering
publisher.none.fl_str_mv Brazilian Society of Chemical Engineering
dc.source.none.fl_str_mv Brazilian Journal of Chemical Engineering v.18 n.3 2001
reponame:Brazilian Journal of Chemical Engineering
instname:Associação Brasileira de Engenharia Química (ABEQ)
instacron:ABEQ
instname_str Associação Brasileira de Engenharia Química (ABEQ)
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reponame_str Brazilian Journal of Chemical Engineering
collection Brazilian Journal of Chemical Engineering
repository.name.fl_str_mv Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)
repository.mail.fl_str_mv rgiudici@usp.br||rgiudici@usp.br
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