Pra Rancangan Pabrik Ethylene Dichloride dari Gas Etilen dan Klorin dengan Proses Direct Chlorination Vapour Phase

Agnetta, Rr. Alvara Dahayunanda (2026) Pra Rancangan Pabrik Ethylene Dichloride dari Gas Etilen dan Klorin dengan Proses Direct Chlorination Vapour Phase. Undergraduate thesis, UPN Veteran Jawa Timur.

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Abstract

The Ethylene Dichloride (EDC) plant using the direct chlorination method is designed with a capacity of 98,000 tons/year, to be established in the Krakatau Industrial Estate, Warnasari, Cilegon, Banten. The main raw materials used are Ethylene (C₂H₄) and Chlorine (Cl₂), while the supporting material used as a catalyst is Ethylene Dibromide (C₂H₄Br₂). The production process consists of a raw material preparation stage, namely pressure reduction and heating of ethylene (C₂H₄) and chlorine (Cl₂) to the reaction temperature, after which chlorine (Cl₂) is passed through ethylene dibromide (C₂H₄Br₂) before entering the reactor. The next stage is the chlorination reaction in a chlorinating tower, which produces ethylene dichloride (C₂H₄Cl₂). The reaction product is then cooled and separated in a separator, where the gas phase is recycled back to the reactor while the liquid phase is purified using a distillation column. The final stage is the purification of ethylene dichloride (C₂H₄Cl₂) as the main product and the recovery of ethylene dibromide (C₂H₄Br₂) for reuse as a catalyst, thereby improving process efficiency. The plant's electricity requirements are supplied by PLN for air conditioning and lighting, while process electricity needs are supplied by a generator set. Water requirements are obtained from KTI Cilegon, Banten, which will be processed in the utility unit for use as process water, cooling water, boiler feed water, and sanitation water. This plant adopts a Limited Liability Company (PT) organizational system, with a line-and-staff organizational structure. The plant is planned to operate continuously, with an annual operating time of 330 days of production. Based on the calculations and discussion that have been carried out, the following conclusions can be drawn: Production Capacity : 98,000 tons/year Company Form : Limited Liability Company (PT) Organizational System : Line and Staff Number of Employees : 153 Operating Time : 330 days/year, 24 hours/day Plant Location : Krakatau Industrial Estate, Warnasari, Cilegon, Banten Plant Area : 25,000 m² Raw Materials a. Ethylene : 8,096.8376 kg/hour b. Chlorine : 20,562.5572 kg/hour c. Ethylene Dibromide : 2,056.2557 kg/hour Ethylene Dichloride Product : 12,373.7373 kg/hour Utilities a. Boiler Feed Water Requirement : 2.6258 m³/hour b. Cooling Water Requirement : 568.4228 m³/hour c. Sanitation Water Requirement : 0.2396 m³/hour d. Electricity Requirement : 896.6297 kWh e. Fuel Requirement : 92.3776 kg/hour Economic Analysis a. Construction Period : 2 years b. Plant Lifetime : 10 years c. Fixed Capital Investment (FCI) : IDR 700,706,571,035 d. Working Capital Investment (WCI) : IDR 490,815,453,351 e. Total Capital Investment (TCI) : IDR 1,202,208,320,568 f. Raw Material Cost/year : IDR 1,659,137,072,188 g. Utility Cost/year : IDR 28,998,350,645 h. Total Production Cost (TPC) : IDR 1,967,412,858,970 i. Sales Revenue : IDR 2,629,928,000,000 j. Bank Loan Interest : 8% k. Rate of Investment (before tax) : 23.11% l. Rate of Investment (after tax) : 18.02% m. Pay Back Period : 3 years 6 months n. Internal Rate of Return (IRR) : 13.1998% o. Break Even Point (BEP) : 28.3%

Item Type: Thesis (Undergraduate)
Contributors:
ContributionContributorsNIDN/NIDKEmail
Thesis advisorErliyanti, Nove KartikaNIDN0723118602nove.kartika.nke.tk@upnjatim.ac.id
Subjects: T Technology > TP Chemical technology > TP155 Chemical engineering
Divisions: Faculty of Engineering > Departement of Chemical Engineering
Depositing User: Ms. Rr. Alvara Dahayunanda Agnetta
Date Deposited: 23 Jul 2026 03:00
Last Modified: 23 Jul 2026 03:37
URI: https://repository.upnjatim.ac.id/id/eprint/57511

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