Pabrik Sorbitol dari Glukosa dengan Proses Hidrogenasi Katalitik Menggunakan Fixed Beed Reactor

Febriyanti, Alda (2022) Pabrik Sorbitol dari Glukosa dengan Proses Hidrogenasi Katalitik Menggunakan Fixed Beed Reactor. Undergraduate thesis, UPN Veteran Jawa Timur.

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Abstract

The Sorbitol factory with a capacity of 70,000 tonnes/year will be established in the Kendal Industrial Estate, Jl. Saptarengga No. 2 A, Tambak, Wonorejo, Kec. Kaliwungu, Kendal Regency, Central Java 51371, Indonesia. The factory operates 24 hours a day and 330 days a year. This Sorbitol factory is made from Glucose taken from PT. Sweet Source of Hope Jaya. Sorbitol is a product that has many uses in various industrial sectors, in the pharmaceutical industry it is used as a surfactant, in the food industry it is used as a sweetener and a mixture in food, and in the cosmetic industry it is used as a humectant and thickening agent in the manufacture of cosmetics. Sorbitol in this design is obtained through a catalytic hydrogenation reaction between glucose and hydrogen gas assisted by a Raney Nickel catalyst. Glucose is stored in the glucose storage warehouse (F-111) transported to the hopper (F-113) using a bucket elevator (J-112), after coming from the hopper it is then put into the dissolution tank (M-110) using a screw conveyor (J-114) and glucose dissolved in water. The glucose solution is then pumped into the heater (E-212) to be heated and the pressure raised using a compressor (G-213) which is then flowed to the catalytic hydrogenation reactor (R-210). Hydrogen gas from the hydrogen storage tank (F-214) is flowed to expander 1 (G-215) to reduce its pressure and then is fed to the catalytic hydrogenation reactor (R-210). A solution of glucose and hydrogen gas reacts and is assisted by a Raney Nickel catalyst in a catalytic hydrogenation reactor to form sorbitol. The sorbitol formed is then pumped to expander 2 (G-312) to reduce its pressure, and to cooler 1 (E-313) to be cooled and flowed to the carbonation tank (D-310) for the decolorization process. After that, the sorbitol solution was pumped into the evaporator (V-320) to concentrate the concentration up to 70%. The 70% sorbitol solution is then pumped into cooler 2 (E-332) to be cooled and flowed to the sorbitol storage tank (F-330). The details of the pre-planned Sorbitol factory based on economic analysis are as follows; capacity : 70,000 tons/year, company form : Limited Liability Company (PT), organizational system : line and staff, number of employees : 158 people, operating system : continuous, operating time : 330 days/year; 24 hours, Fixed Capital Investment (FCI) : IDR 304,547,520,433, Working Capital Investment (WCI) : IDR 244,678,519,060, Total Production Cost (TPC) : IDR 1,133,928,869,966, Pay Back Period : 3 years 9 months, Bank loan interest : 8%, Return of Investment (before tax) : 24.77%, Return of Investment (after tax) : 18.58%, Internal Rate of Return : 12.4%, Break Even Point : 34.47 %.

Item Type: Thesis (Undergraduate)
Contributors:
ContributionContributorsNIDN/NIDKEmail
Thesis advisorSaputro, Erwan AdiNIDN0010048001erwanadi.tk@upnjatim.ac.id
Subjects: T Technology > TP Chemical technology > TP155 Chemical engineering
Divisions: Faculty of Engineering > Departement of Chemical Engineering
Depositing User: Alda Febriyanti
Date Deposited: 14 Nov 2022 03:14
Last Modified: 14 Nov 2022 03:14
URI: http://repository.upnjatim.ac.id/id/eprint/10185

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