Digital Library: No conditions. Results ordered -Date Deposited. 2024-03-29T13:23:47ZEPrintshttp://digilib.unila.ac.id/images/sitelogo.pnghttp://digilib.unila.ac.id/2018-02-07T08:06:26Z2018-02-07T08:06:26Zhttp://digilib.unila.ac.id/id/eprint/30235This item is in the repository with the URL: http://digilib.unila.ac.id/id/eprint/302352018-02-07T08:06:26Z
PRARANCANGAN PABRIK ANILIN DARI HIDROGENASI
NITROBENZEN FASE UAP KAPASITAS 30.000 TON/TAHUN
(Perancangan Menara Distilasi-306 (MD-306))
ABSTRAK
PRARANCANGAN PABRIK ANILIN DARI HIDROGENASI
NITROBENZEN FASE UAP KAPASITAS 30.000 TON/TAHUN
(Perancangan Menara Distilasi-306 (MD-306))
Oleh
Wildan Arief Rohdina
Anilin merupakan salah satu produk industri kimia yang digunakan sebagai bahan
baku pembuatan Isocynates, Prekursor, Bahan Pembuatan Pestisida, Hidroquinon,
pembuatan Metilen Dianilin. Anilin dapat diproduksi dengan beberapa proses yaitu
1) Proses Hidrogenasi Nitrobenzen Fase Uap, 2) Proses Aminasi Phenol dan 3)
Proses Aminasi Chlorobenzene. Penyediaan kebutuhan utilitas pabrik berupa sistem
pengolahan dan penyediaan air, sistem penyediaan steam, cooling water, dan sistem
pembangkit tenaga listrik.
Kapasitas produksi pabrik Aniline direncanakan 30.000 ton/tahun dengan 330 hari
kerja dalam 1 tahun. Lokasi pabrik direncanakan didirikan di daerah Cilegon,
Banten. Tenaga kerja yang dibutuhkan sebanyak 135 orang dengan bentuk badan
usaha Perseroan Terbatas (PT) dengan struktur organisasi line and staff.
Dari analisisekonomi diperoleh:
Fixed Capital Investment (FCI) = Rp 325.814.580.114
Working Capital Investment (WCI) = Rp 57.496.690.608
Total Capital Investment (TCI) = Rp 383.311.270.723
Break Even Point (BEP) = 35,98%
Shut Down Point (SDP) = 22,1%
Pay Out Time before taxes (POT)
b
= 3,38 years
Pay Out Time after taxes (POT)
a
= 4,06 years
Return onInvestment before taxes (ROI)
b
= 46,12%
Return onInvestment after taxes (ROI)
a
= 36,9%
Discounted cash flow (DCF) = 20,94%
Berdasarkan beberapa paparan di atas, maka pendirian pabrik aniline ini layak
untuk dikaji lebih lanjut, karena merupakan pabrik yang menguntungkan dari sisi
ekonomi dan mempunyai prospek yang relatif cukup baik.
ABSTRACT
PREDESIGN OF ANILIN FROM VAPOUR PHASE NITROBENZEN
HIDROGENATION CAPACITY 30.000 TONS/YEARS
(Design Distillation Column-306 (MD-306))
By
Wildan Arief Rohdina
Aniline is one of the product industry chemicals are used as the raw materials for
Isocynates, Precursor, pesticide, Hidroquinon, Metilen Dianilin. Aniline can be
produced by some of the process is : 1) Process of Vapour phase nitrobenzen
hidrogenation, 2) Procces from Phenol Amination and 3) Procces from
Chlorobenzene Amination. Provision of utility plant needs a treatment system and
water supply, cooling water, ,dan Generator electrical power system.
Capacity of the plant is planned to production aniline is 30.000 tons/year with 330
working days in a year. The location of plant is planned in Cilegon, Banten. Labor
needed in this plant as many as 135 people with a business entityform Limited
Liability Company (PT) with line and staff organizational structure.
From teh economic analysis is obtained :
Fixed Capital Investment (FCI) = Rp 325.814.580.114
Working Capital Investment (WCI) = Rp 57.496.690.608
Total Capital Investment (TCI) = Rp 383.311.270.723
Break Even Point (BEP) = 35,98%
Shut Down Point (SDP) = 22,1%
Pay Out Time before taxes (POT)
b
= 3,38 years
Pay Out Time after taxes (POT)
a
= 4,06 years
Return onInvestment before taxes (ROI)
b
= 46,12%
Return onInvestment after taxes (ROI)
a
= 36,9%
Discounted cash flow (DCF) = 20,94%
By considering above the summary, it is proper establishment of aniline plant for
studied further, because the plant is profitable and has good prospects future.1015041054 Wildan Arief Rohdinawildanariefrohdina@yahoo.com