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dc.contributor.advisorBulan, Rumondang
dc.contributor.authorButar-Butar, Pujiman
dc.date.accessioned2022-12-09T08:59:20Z
dc.date.available2022-12-09T08:59:20Z
dc.date.issued2008
dc.identifier.urihttps://repositori.usu.ac.id/handle/123456789/72188
dc.description.abstractWhitening pulp and lignin separation from cellulosa is a big of part happen on DO-Tower step is additionally ClO2 with range concentrate 0,75-0,78 % and pulp consistency is around 4,5 %. On this step, the pulp stock flow must be accorded with ClO2 flow because flow rate of ClO2 is very in fluence to increase brightness degree, and losing the dirts of pulp. On this step if the using of clorin dioxida is not axcatly enoungh is not perfect enough is dispoised will be make the clor of pulp will be drak, the caused of the failure to lose the companents of lignin compound, but the if using is the too many and will lose out the company.en_US
dc.language.isoiden_US
dc.publisherUniversitas Sumatera Utaraen_US
dc.titlePengaruh Laju Alir Pulp terhadap Konsentrasi ClO2 untuk Meningkatkan % Brightness Pulp di Do-Tower di PT. Toba Pulp Lestari, Tbk Porseaen_US
dc.typeThesisen_US
dc.identifier.nimNIM052409040
dc.identifier.nidnNIDN0030085402
dc.identifier.kodeprodiKODEPRODI47401#Kimia
dc.description.pages45 Halamanen_US
dc.description.typeKertas Karya Diplomaen_US


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