Please use this identifier to cite or link to this item: http://repository.iti.ac.id/jspui/handle/123456789/2568
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dc.contributor.authorAlamsyah, Ridho Anugrah-
dc.contributor.authorJeses Padua, Mercynov Gloryan-
dc.contributor.authorRatnawati, Ratnawati-
dc.date.accessioned2024-10-25T08:20:07Z-
dc.date.available2024-10-25T08:20:07Z-
dc.date.issued2024-09-03-
dc.identifier.urihttp://repository.iti.ac.id/jspui/handle/123456789/2568-
dc.descriptionDosen Pembimbing : Ratnawatien_US
dc.description.abstractIndustrial development in Indonesia has increased very rapidly from year to year, especially in the chemical industry. One of them is Glycerol Monostearate, an organic compound that is widely used in the food, cosmetic, and pharmaceutical industries, especially in the bakery industry, Glycerol Monostearate is used as an emulsifier to maintain emulsion stability and reduce surface tension so that the texture of food is getting better. Glycerol Monostearate consumption in Indonesia is projected to reach 13,470 tons by 2027. This can be an opportunity to establish a Glycerol Monostearate plant to reduce imports and increase foreign exchange by increasing exports. The Glycerol Monostearate plant is designed with a capacity of 15,000 tons per year. The raw materials used to produce Glycerol Monostearate are Glycerol and Stearic Acid with Sodium Hydroxide catalyst. This plant will be established in Jalan Raya Manyar KM 11 Manyarejo, Manyar Sido Rukun, Manyar, Gresik, Jawa Timur which is operated continuously. The production process of Glycerol Monostearate in this plant has two main stages, namely reaction and purification. In the Esterification Reactor (CSTR) there will be an esterification reaction at a temperature of 250 o C and a pressure of 3.4 atm with isothermal operating conditions to form Glycerol Monostearate. For the purification stage, Glycerol Monostearate is separated from Glycerol, Stearic Acid and Sodium Hydroxide as by-products using a 2-stage crystallization method at 125 o o C and 90 C with a pressure of 1 atm until the purity of Glycerol Monostearate is 91.8% and stored in the product holding tank. The Glycerol Monostearate plant requires utility units including water, electricity, and diesel fuel. Water needs come from JIIPE Area water as much as 19.107 liter/hour for start-up needs and 960 liter/hour for continuous needs. Electricity needs come from PLN reaching 161 kWh. Diesel fuel needs come from PT Pertamina amounting to 50 liters/hour. The legal form of this company is a Limited Liability Company (PT) with the organizational structure used is a line and staff system. The company is led by a director with 164 employees. Employees consist of shift employees and non-shift employees who work according to working hours. The factory operates for 330 days a year. Based on the results of the economic analysis carried out with a bank interest rate of 10%, it is as follows : a. Total Capital Investment = IDR 337.000.000.000 b. Own Capital (74,80%) = IDR 252.000.000.000 c. Bank Loans (25,20%) = IDR 85.000.000.000 Interest Rate = 10% Loan Period = 5 years d. Break Even Point (BEP) first year = 56% e. Minimum Payback Period (MPP) = 5 years f. Internal Rate of Return (IRR) = 28,11 % g. Net Cash Flow at Present Value = IDR 420.000.000.000 Based on the results of the economic analysis carried out, it can be concluded that this propylene glycol plant is feasible to be established.en_US
dc.language.isootheren_US
dc.publisherINSTITUT TEKNOLOGI INDONESIAen_US
dc.subjectGlycerol Monostearate.en_US
dc.subjectGlycerolen_US
dc.subjectStearic Aciden_US
dc.subjectEsterificationen_US
dc.titlePra rancangan Pabrik Gliserol Monostearat Kapasitas 15.000 Ton/Tahunen_US
dc.typeThesisen_US
dc.identifier.nidnNIDN0301036303-
dc.identifier.nimNIM11420000007-
dc.identifier.nimNIM11420000008-
dc.identifier.kodeprodiKODEPRODI24201#Teknik Kimia-
Appears in Collections:[TA] Teknik Kimia

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2 ABSTRAK GLISEROL MONOSTEARAT.pdfABSTRAK148.1 kBAdobe PDFView/Open
3 BAB 1 GLISEROL MONOSTEARAT.pdfBAB I612.97 kBAdobe PDFView/Open
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9 DAFTAR PUSTAKA GLISEROL MONOSTEARAT.pdfDAFTAR PUSTAKA129.79 kBAdobe PDFView/Open
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