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dc.contributor.advisorTaslim
dc.contributor.authorYuliantika, Yesi
dc.date.accessioned2023-10-09T02:57:56Z
dc.date.available2023-10-09T02:57:56Z
dc.date.issued2023
dc.identifier.urihttps://repositori.usu.ac.id/handle/123456789/88016
dc.description.abstractOne alternative utilization of the nipa plant is to make it as a raw material for producing bioethanol. The glucose contained in the nipa sap can produce bioethanol with an alcohol content of 99,5% (Fuel Grade Ethanol). The preliminary plant design of bioethanol from nipa sap by the fermentation process has a production capacity of 17.500 tons/year and operates for 330 days a year. The main process in this plant design consists of three stages, namely the raw material pretreatment stage, the product formation stage, and the product purification stage. In fermentation stage, 4 units of fermentation reactors were used which operated at 30°C for 32 hours. The amount of nipa sap needed to achieve annual production capacity is 106.405,90 tonnes/year. The specific task was solved for the detailed engineering design of a distillation column for bioethanol purification. The distillation column that has been designed has the following specifications: • Number of trays : 30 trays • Feed-in tray : Tray 10th from the bottom • Distillation column height : 15,50 m • Diameter of distillation column : 0,69 m • Distillation column shell material : Carbon steel SA-283 grade C • Distillation column shell thickness: 3/16 in • Distillation column head thickness : 3/16 in • Distillation column tray material : Carbon Steel Manufacturing bioethanol from nipa sap by the fermentation process is planned to be built in Indragiri Hilir Regency, Riau Province, with a total plant area of 19.3332 m2. The water requirement for this plant is supplied from the Asahan River as much as 130.556.71 kg/batch. The planned company organizational form is Perseroan Terbatas (PT) with a line and staff organizational structure, and a total of 150 employees. The results of the economic analysis on this preliminary plant design are as follows:  Capital Investment (CI) = IDR 592,286,550,974  Total Cost (TC) = IDR 400,878,035,516  Profit Margin (PM) = 21.28 %  Break Even Point (BEP) = 44.71 %  Return on Investment (ROI) = 20.74 %  Return On Network (RON) = 34.56 %  Pay Out Time (POT) = 4 years 3 months  Internal Rate of Return (IRR) = 27.62 % Based on the results of economic analysis, it can be concluded that the bioethanol manufacturing plant from nipa sap with a fermentation process is feasible to establish.en_US
dc.language.isoiden_US
dc.publisherUniversitas Sumatera Utaraen_US
dc.subjectbioethanolen_US
dc.subjectfuel grade ethanolen_US
dc.subjectfermentationen_US
dc.subjectdistillation coloumnen_US
dc.subjectSDGsen_US
dc.titlePra Rancangan Pabrik Pembuatan Bioetanol 99,5% (Fuel Grade Ethanol) dari Nira Nipah (Nypa Fructicans) dengan Kapasitas 17.500 Ton/ Tahun dan Tugas Khusus: Rancangan Keteknikan Detail Kolom Distilasien_US
dc.typeThesisen_US
dc.identifier.nimNIM180405016
dc.identifier.nidnNIDN0015016502
dc.identifier.kodeprodiKODEPRODI24201#Teknik Kimia
dc.description.pages461 Halamanen_US
dc.description.typeSkripsi Sarjanaen_US


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