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dc.contributor.advisorBulan, Rumondang
dc.contributor.authorManalu, Herdianus
dc.date.accessioned2022-12-10T08:21:31Z
dc.date.available2022-12-10T08:21:31Z
dc.date.issued2011
dc.identifier.urihttps://repositori.usu.ac.id/handle/123456789/72445
dc.description.abstractBleaching Proses in PT. Toba Pulp Lestari, Tbk Porsea uses ClO2 as material bleaching to disappearing or whitening color substance of pulp. Remained lignine is very dominan substance to make coloring of the pulp, therefore it must be eliminated. If much more ClO2 uses at bleaching process, specifically at D1 stage, it will make much more brightness too. The usage of ClO2 at pulp process be equal to the amount of lignine to be eliminated from the pulp. The concentration is not too high, so it will not show environment emition. Because of, moreover decrease of environment emition and decrease consumstion of ClO2 so, increasing of O2 need protect for sellulosa in pulp. Standart of quality of pulp brightness uses at D1 Stage is 88-90% ISO and ClO2 concentration at D1 stage is 7-8 gram/literen_US
dc.language.isoiden_US
dc.publisherUniversitas Sumatera Utaraen_US
dc.titlePengaruh Penambahan Oksigen (O2) pada Tower Eop Terhadap Jumlah Pemakaian Klorin Dioksida (Clo2) pada Tower D1 di Unit Bleaching di PT. Toba Pulp Lestari,Tbk Poren_US
dc.typeThesisen_US
dc.identifier.nimNIM082409002
dc.identifier.nidnNIDN0030085402
dc.identifier.kodeprodiKODEPRODI47401#Kimia
dc.description.pages50 Halamanen_US
dc.description.typeKertas Karya Diplomaen_US


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