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dc.contributor.advisorMasyithah, Zuhrina
dc.contributor.authorSari, Indah Mutya
dc.date.accessioned2025-02-12T08:36:13Z
dc.date.available2025-02-12T08:36:13Z
dc.date.issued2024
dc.identifier.urihttps://repositori.usu.ac.id/handle/123456789/101196
dc.description.abstractPre-design of the cyclohexane production plant from benzene and hydrogen through a hydrogenation process has a production capacity of 140.000 tons per year and operates for 330 days per year. The main process in this plant's preliminary design consists of three stages: raw material preparation, benzene hydrogenation, and product separation and purification. The amount of benzene required to reach the annual production capacity is 17.331.386 kg/hour. This cyclohexane production plant, utilizing a hydrogenation process from benzene and hydrogen, is planned to be established in the Krakatau Steel Industrial Area, Cilegon, West Java, with a total plant area of 21.061 m². The water requirements for the plant will be supplied by PT Krakatau Tirta Industri at a rate of 367.803.873 kg/hour. The planned company organization form is a Limited Liability Company (PT) with a line and staff organizational structure, employing a total of 99 peoples. The economic evaluation shows an investment capital (CI) of IDR 697.349.494.906, total production costs of IDR 2.899.774.328.505, and sales of IDR 3.505.756.090.994, with a net profit of IDR 456.281.267.073. The profit margin is 37,35%, ROI is 32,58%, and IRR is 52,2%. The project is projected to break even (BEP) at 36,1% of the capacity, with an investment payback period (POT) of 2 years and 2 months. Based on the economic analysis, the preliminary design of this plant is considered feasible for realization.en_US
dc.language.isoiden_US
dc.publisherUniversitas Sumatera Utaraen_US
dc.subjectBenzeneen_US
dc.subjectHydrogenation Processen_US
dc.subjectCyclohexaneen_US
dc.titlePra Rancangan Pabrik Sikloheksana dari Benzena dan Hidrogen dengan Proses Hidrogenasi Menggunakan Katalis Paladium Kapasitas 140.000 Ton/Tahunen_US
dc.title.alternativePreliminary Design of a Cyclohexane Plant from Benzene and Hydrogen through Hydrogenation Process Using a Palladium Catalyst with a Capacity of 140.000 Tons/Yearen_US
dc.typeThesisen_US
dc.identifier.nimNIM200405016
dc.identifier.nidnNIDN0005097101
dc.identifier.kodeprodiKODEPRODI24201#Teknik Kimia
dc.description.pages582 Pagesen_US
dc.description.typeSkripsi Sarjanaen_US
dc.subject.sdgsSDGs 9. Industry Innovation And Infrastructureen_US


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