Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances
Autor(a) principal: | |
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Data de Publicação: | 2011 |
Outros Autores: | , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Brazilian Journal of Chemical Engineering |
Texto Completo: | http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000300011 |
Resumo: | Thin film composite membranes were prepared by using1,3 - phenylene diamine in the gelation bath as well as in coating conditions. The cross - sectional view of the membranes shows different patterns for membranes prepared in a water - bath (Mem - I) and a diamine - containing water bath (Mem - II). The thin film composite membranes prepared using a diamine bath and coating (Mem - III) had improved salt rejecting ability but low volume flux. The performances of the salt rejection follows the order Na2SO4 > NaCl > MgSO4> MgCl2, as expected. The salt separation performances of the membranes made with higher concentration of 1,3 phenylene diamine follow the order Mem - IIIb > Mem - I > Mem - IIb. For membranes made with low concentration of 1,3 - phenylene diamine, the salt separation follows the same trend, (Mem - IIIa > Mem - IIa). |
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Brazilian Journal of Chemical Engineering |
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Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performancesMembraneThin film composite1,3-phenylene diamineGelation bathThin film composite membranes were prepared by using1,3 - phenylene diamine in the gelation bath as well as in coating conditions. The cross - sectional view of the membranes shows different patterns for membranes prepared in a water - bath (Mem - I) and a diamine - containing water bath (Mem - II). The thin film composite membranes prepared using a diamine bath and coating (Mem - III) had improved salt rejecting ability but low volume flux. The performances of the salt rejection follows the order Na2SO4 > NaCl > MgSO4> MgCl2, as expected. The salt separation performances of the membranes made with higher concentration of 1,3 phenylene diamine follow the order Mem - IIIb > Mem - I > Mem - IIb. For membranes made with low concentration of 1,3 - phenylene diamine, the salt separation follows the same trend, (Mem - IIIa > Mem - IIa).Brazilian Society of Chemical Engineering2011-09-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000300011Brazilian Journal of Chemical Engineering v.28 n.3 2011reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322011000300011info:eu-repo/semantics/openAccessJoshi,R. NSingh,KBhattacharya,Aeng2011-09-01T00:00:00Zoai:scielo:S0104-66322011000300011Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2011-09-01T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false |
dc.title.none.fl_str_mv |
Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances |
title |
Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances |
spellingShingle |
Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances Joshi,R. N Membrane Thin film composite 1,3-phenylene diamine Gelation bath |
title_short |
Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances |
title_full |
Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances |
title_fullStr |
Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances |
title_full_unstemmed |
Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances |
title_sort |
Approaches to prepare tfc polyamide membranes by coating diamine during, and/or post formation of asymmetric membranes and their performances |
author |
Joshi,R. N |
author_facet |
Joshi,R. N Singh,K Bhattacharya,A |
author_role |
author |
author2 |
Singh,K Bhattacharya,A |
author2_role |
author author |
dc.contributor.author.fl_str_mv |
Joshi,R. N Singh,K Bhattacharya,A |
dc.subject.por.fl_str_mv |
Membrane Thin film composite 1,3-phenylene diamine Gelation bath |
topic |
Membrane Thin film composite 1,3-phenylene diamine Gelation bath |
description |
Thin film composite membranes were prepared by using1,3 - phenylene diamine in the gelation bath as well as in coating conditions. The cross - sectional view of the membranes shows different patterns for membranes prepared in a water - bath (Mem - I) and a diamine - containing water bath (Mem - II). The thin film composite membranes prepared using a diamine bath and coating (Mem - III) had improved salt rejecting ability but low volume flux. The performances of the salt rejection follows the order Na2SO4 > NaCl > MgSO4> MgCl2, as expected. The salt separation performances of the membranes made with higher concentration of 1,3 phenylene diamine follow the order Mem - IIIb > Mem - I > Mem - IIb. For membranes made with low concentration of 1,3 - phenylene diamine, the salt separation follows the same trend, (Mem - IIIa > Mem - IIa). |
publishDate |
2011 |
dc.date.none.fl_str_mv |
2011-09-01 |
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=S0104-66322011000300011 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322011000300011 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/S0104-66322011000300011 |
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.28 n.3 2011 reponame:Brazilian Journal of Chemical Engineering instname:Associação Brasileira de Engenharia Química (ABEQ) instacron:ABEQ |
instname_str |
Associação Brasileira de Engenharia Química (ABEQ) |
instacron_str |
ABEQ |
institution |
ABEQ |
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 |
_version_ |
1754213173482749952 |