PRA RENCANA PABRIK PEMBUATAN MONOMER STIRENA DENGAN KAPASITAS PRODUKSI 160.000 TON/TAHUN

SETIAWAN, REDI and HANDOKO, AHMAD and Novia, Novia (2019) PRA RENCANA PABRIK PEMBUATAN MONOMER STIRENA DENGAN KAPASITAS PRODUKSI 160.000 TON/TAHUN. Undergraduate thesis, Sriwijaya University.

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Abstract

The Styrene Monomer Plant is planned to be located in the area of East Kalimantan, covering an area of 6 hectares with a capacity of 160,000 tons / year. The process of making this Stirena Monomer uses the raw material Methanol and Toluene with Copper Oxide as a catalyst. The reaction takes place at a pressure of 1.5 atm and a temperature of 550 C (US 9,272,962 B2). The reactor used is a Multitubular Fixed Bed Reactor. With the reaction that occurs as follows: o Reaction 1 : CH3OH + ½ O2 CH2O + H2O Reaction 2 : CH2O + C7H8 C8H8 + H2O The company is a Limited Liability Company (PT) with a Line and Staff organizational structure, which is led by a President Director with 169 employees. The results of economic analysis, the Styrene Monomer manufacturing plant made from Methanol and Toluene is declared feasible to be established. Based on economic analysis as follows: • Total Capital Investment (TCI) : US$ 30.884.796,225 • Total Production Cost (TPC) : US$ 1.066.0598.903,7242 • Total Sales per Year (SP) : US$ 1.096.343.498,1103 • Annual Cash Flow : US$ 23.446.423,7494 • Pay Out Time : 1,2664 years • Rate of Return : 67,4157% • Break Even Point : 37,59% • Service Life : 11 years Keywords: Styrene Monomer, Methanol, Toluene, Copper Oxide, Oxidation

Item Type:	Thesis (Undergraduate)
Uncontrolled Keywords:	Monomer Stirena, Metanol, Toluene, Oksidasi Metanol
Subjects:	T Technology > TP Chemical technology > TP155-156 Chemical engineering
Divisions:	03-Faculty of Engineering > 24201-Chemical Engineering (S1)
Depositing User:	Users 1724 not found.
Date Deposited:	06 Sep 2019 03:34
Last Modified:	06 Sep 2019 03:34
URI:	http://repository.unsri.ac.id/id/eprint/6455

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