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dc.contributor.authorHUMAIDI, Fakhri Arkan
dc.date.accessioned2024-07-17T03:00:32Z
dc.date.available2024-07-17T03:00:32Z
dc.date.issued2023-06-16
dc.identifier.nim191910401066en_US
dc.identifier.urihttps://repository.unej.ac.id/xmlui/handle/123456789/122500
dc.description.abstractButyl acetate plant design from butanol and acetic acid with a production capacity of 35,000 tons/year. The raw materials used are butanol and acetic acid with amberlyst 15 catalyst support. This factory will be established in JIIPE, Gresik, East Java with a production time of 330 days/year. The production process consists of raw material preparation, esterification reaction, and purification. The esterification reaction took place in the fluidized bed CSTR reactor with operating conditions of 90°C, 1 atm pressure, and 90 minutes of reaction time. Product purification is carried out in a flash drum to obtain a product purity of 99.5% butyl acetate. Process support utilities include water requirement of 191.128 m3 /day, steam requirement of 1364.796 kg/hour, brine requirement of 37263.27 kg/hour, electricity requirement of 125.76 kWh and fuel of 549.34 lb/hour. The form of company chosen is a Limited Liability Company (PT) with a total of 153 employees consisting of shift and non-shift employees. Based on economic evaluation, Annual cash flow (ACF) is 45%, Pay Out Time (POT) is 2.5 years, and Break Event Point (BEP) is 44.81%.en_US
dc.language.isootheren_US
dc.publisherFakultas Tekniken_US
dc.subjectButyl Acetateen_US
dc.subjectEsterificationen_US
dc.subjectFluidized Bed CSTRen_US
dc.titlePra Rancangan Pabrik Butil Asetat dari Butanol dan Asam Asetat dengan Kapasitas 35.000 Ton/Tahunen_US
dc.typeOtheren_US
dc.identifier.prodiPogram Studi Teknik Kimiaen_US
dc.identifier.pembimbing1Ir. Boy Arief Fachri S.T., M.T., Ph.D., IPM.en_US
dc.identifier.pembimbing2Ir. Bekti Palupi S.T., M.Eng.en_US
dc.identifier.validatorvalidasi_repo_iswahyudi_Mei_2024en_US
dc.identifier.finalization0a67b73d_2024_07_tanggal 10en_US


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