PRA RENCANA PABRIK PEMBUATAN PARAXYLENE DENGAN PROSES ISOMERISASI XYLENE KAPASITAS PRODUKSI 450.000 TON/TAHUN

FADHILAH, AFINA and PERMATA, ADELLIA INDAH and Hadiah, Fitri (2018) PRA RENCANA PABRIK PEMBUATAN PARAXYLENE DENGAN PROSES ISOMERISASI XYLENE KAPASITAS PRODUKSI 450.000 TON/TAHUN. Undergraduate thesis, Sriwijaya University.

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Abstract

Pabrik Paraxylene direncanakan berlokasi di daerah Cilegon, Banten. Pabrik ini meliputi area seluas 8 Ha dengan kapasitas 450.000 ton per tahun. Proses pembuatan Paraxylene dilakukan dengan proses isomerisasi xylene di dalam Reaktor-01 (R-01) pada temperatur 260oC dengan tekanan 20 atm pada fase liquid dan pada Reaktor-02 (R-02) pada temperatur 343,3 oC dengan tekanan 1,7 atm pada fase gas reaksi yang terjadi adalah sebagai berikut : C8H10 (mX) C8H10 (oX) C8H10 (oX) C8H10 (pX) Pabrik ini merupakan perusahaan yang berbentuk Perseroan Terbatas (PT) dengan sistem organisasi line and staff, yang dipimpin oleh seorang direktur utama dengan jumlah karyawan 167 orang. Berdasarkan hasil analisa ekonomi, maka Pabrik Paraxylene ini dinyatakan layak didirikan : a. Annual Cash Flow = US $ 64.103.436,30 b. Hasil penjualan per tahun = US $ 739.000.367,49 c. Biaya produksi per tahun = US $ 654.261.675,10 d. Pay out time = 1,13 tahun e. Rate of return on investment = 89,23 % f. Break evenpoint = 34 % g. Service life = 11 tahun

Item Type:	Thesis (Undergraduate)
Uncontrolled Keywords:	Paraxylene, isomerisasi xylene, line and staff
Subjects:	T Technology > TP Chemical technology > TP155-156 Chemical engineering
Divisions:	03-Faculty of Engineering > 24201-Chemical Engineering (S1)
Depositing User:	Users 2715 not found.
Date Deposited:	07 Nov 2019 07:57
Last Modified:	07 Nov 2019 07:57
URI:	http://repository.unsri.ac.id/id/eprint/15372

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