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dc.contributor.advisorSinaga, Mersi Suriani
dc.contributor.authorBatubara, Lidya Novita Esfranza Br
dc.date.accessioned2025-03-04T07:02:51Z
dc.date.available2025-03-04T07:02:51Z
dc.date.issued2024
dc.identifier.urihttps://repositori.usu.ac.id/handle/123456789/101773
dc.description.abstractBio-oil is a blackish liquid fuel that comes from biomass such as wood, rice straw, empty oil palm fruit bunches, corn cob bark and other biomass from forestry waste and the forest products industry through pyrolysis technology (Wibowo, 2013). Bio-oil is a very promising renewable energy source that is used for industries such as combustion fuel, power generation, to produce chemicals, resins, and can be mixed with diesel oil as diesel engine fuel with certain mixtures (Saputra and Syaiful, 2015). The potential for bio-oil to be useful as a raw material and support for the chemical industry has made bio-oil widely used, especially in Indonesia. Therefore, an effort is needed so that bio-oil production can be fulfilled by establishing a bio-oil factory in Indonesia. The design of this bio-oil factory uses cocoa shell as the main raw material, which is obtained from farmers' production waste, where cocoa shell is able to produce bio-oil from fast pyrolysis. The first process carried out was the Pre- Treatment process for the raw material, namely cocoa shell in the storage warehouse (G-101). Next, the cocoa shell is fed to a rotary cutter (RC-101) to reduce the size, after that it is fed to a rotary dryer (DE-101) to reduce the water content of the cocoa shell raw material. The dried cocoa is fed into a disk mill (DM- 101) to make it smaller in size so that it meets the criteria for using a fluidized bed reactor and to speed up the pyrolysis reaction. Powdered cocoa shell is put into a vibrating screen (S-101) to separate the powder from any remaining impurities. Next, the dry and clean powdered cocoa shell is then stored in the rice straw powder bin (TT-101). It is then fed into the fluidized bed reactor (R-201) from the side of the reactor. Next, nitrogen will be fed into the reactor which functions as a fluidizer and oxygen binder. The temperature used in the reactor is 500 ℃. The gas that has been condensed in the condenser will then flow to the knock out drum (D-201) to separate the gas and liquid that is formed. The condensed liquid is what is called bio-oil. Pre-design of this bio-oil factory using cocoa shell as raw material is planned to produce with a production capacity of 38,000 tons/year and operate for 330 days a year. The factory location is planned Bolano Lambunu District, Parigi Moutong Regency, Central Sulawesi Province, Indonesia. The land area required to establish the factory is 19,266.5 m2. The factory's utility water needs will be supplied from the Muara Dua river as much as 11,634.598 kg/hour. The company's organizational form is planned to be a Limited Liability Company (PT) with a total number of employees of 156 people. The results of the economic aspect analysis obtained are as follows: 1. Capital Investment (CI) : $ 76.714.495,83 2. Total Cost (TC) : $ 90.216.247,10 3. Profit Margin (PM) : 15,96% 4. Break Event Point (BEP) : 42,22% 5. Return On Investment (ROI) : 35% 6. Pay Out Time (POT) : 7,545 year 7. Profit Margin (PM) : 33,78% 8. Internal Rate of Return (IRR) : 19% On the results of the analysis of economic aspects, it can be concluded that “A factory for making Bio-oil from cacao shell with a capacity of 38,000 tons/year” is feasible to be established.en_US
dc.language.isoiden_US
dc.publisherUniversitas Sumatera Utaraen_US
dc.subjectBio-oilen_US
dc.subjectFast Pyrolysis Processen_US
dc.subjectCacao Shellen_US
dc.titlePra Rancangan Pabrik Pembuatan Bio-Oil dengan Bahan Baku Limbah Kulit Kakao (Theobrema cacao L.) melalui Proses Pirolisis Cepat dengan Kapasitas Produksi 38.000 Ton/Tahunen_US
dc.title.alternativePre-Design of a Bio-Oil Manufacturing Factory Using the Raw Material of Cocoa Hell Waste (Theobrema cacao L.) through a Fast Pyrolysis Process with a Production Capacity of 38,000 Ton/Yearen_US
dc.typeThesisen_US
dc.identifier.nimNIM180405180
dc.identifier.nidnNIDN0006086806
dc.identifier.kodeprodiKODEPRODI24201#Teknik Kimia
dc.description.pages446 Pagesen_US
dc.description.typeSkripsi Sarjanaen_US
dc.subject.sdgsSDGs 9. Industry Innovation And Infrastructureen_US


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