Branqueamento de polpa celulósica kraft de eucalipto com peróxido ácido ativado por molibdênio

dc.contributor.authorRabelo, Marcos Sousa
dc.contributor.authorSilva, Vanessa Lopes
dc.contributor.authorBarros, Denise Pires de
dc.contributor.authorColodette, Jorge Luiz
dc.contributor.authorSacon, Vera Maria
dc.contributor.authorSilva, Marcelo Rodrigues da
dc.date.accessioned2019-04-26T17:47:25Z
dc.date.available2019-04-26T17:47:25Z
dc.date.issued2009
dc.description.abstractOptimum conditions to run the P Mo stage for bleaching eucalyptus kraft pulp were 90 oC, pH 3.5, 2 h, 0.1 kg/t Mo and 5 kg/t H 2 O 2 . The P Mo stage efficiency increased with decreasing pH (1.5-5.5) and increasing temperature (75-90 °C), time (2-4 h), and hydrogen peroxide (3-10 kg/t) and molybdenum concentration (0.1-0.4 kg/t). The implementation of the P Mo stage, as replacement for the A stage, decreased total active chlorine demand of the OAZDP sequence by 6 kg/t to reach 90% ISO, both in laboratory and mill scale. Such practice resulted in decreased bleaching chemical costs to produce fully bleached pulp of 90% ISO.en
dc.formatpdfpt-BR
dc.identifier.issn1678-7064
dc.identifier.urihttp://dx.doi.org/10.1590/S0100-40422009000500002
dc.identifier.urihttp://www.locus.ufv.br/handle/123456789/24819
dc.language.isoporpt-BR
dc.publisherQuímica Novapt-BR
dc.relation.ispartofseriesv. 32, n. 5, p. 1095-1098, 2009pt-BR
dc.rightsOpen Accesspt-BR
dc.subjectHydrogen peroxidept-BR
dc.subjectMolybdenumpt-BR
dc.subjectPulp bleachingpt-BR
dc.titleBranqueamento de polpa celulósica kraft de eucalipto com peróxido ácido ativado por molibdêniopt-BR
dc.typeArtigopt-BR

Files

Original bundle

Now showing 1 - 1 of 1
Loading...
Thumbnail Image
Name:
artigo.pdf
Size:
202.9 KB
Format:
Adobe Portable Document Format
Description:
artigo

License bundle

Now showing 1 - 1 of 1
Loading...
Thumbnail Image
Name:
license.txt
Size:
1.71 KB
Format:
Item-specific license agreed upon to submission
Description: