TY  - GEN
CY  - UNIVERSITAS LAMPUNG
ID  - eprints57000
UR  - http://digilib.unila.ac.id/57000/
A1  - ZULFA FAUZIYYAH, 1215041057
Y1  - 2019///
N2  - Pabrik Maleic Anhydride berbahan baku n-butana dan oksigen, akan
didirikan di Cilacap, Jawa Tengah. Pabrik ini berdiri dengan mempertimbangkan
ketersediaan bahan baku, sarana transportasi yang memadai, tenaga kerja yang
mudah didapatkan dan kondisi lingkungan.
Pabrik direncanakan memproduksi Maleic Anhydride sebanyak 20.000
ton/tahun, dengan waktu operasi 24 jam/hari, 330 hari/tahun. Bahan baku yang
digunakan adalah n-butana sebanyak 2.116,50 kg/jam dan Vanadium phosphorus
oxcide sebanyak 29.186,5629 kg/jam.
Penyediaan kebutuhan utilitas pabrik Maleic Anhydride berupa:
pengadaan air, pengadaan listrik, kebutuhan bahan bakar, dan pengadaan udara
kering.
Bentuk perusahaan adalah Perseroan Terbatas (PT) menggunakan struktur
organisasi line dan staff dengan jumlah karyawan sebanyak 137 orang.
Dari analisis ekonomi diperoleh:
Fixed Capital Investment (FCI) = Rp 440.396.823.280,-
Working Capital Investment (WCI) = Rp 77.717.086.461,-
Total Capital Investment (TCI) = Rp 518.113,909.742,-
Break Even Point (BEP) = 50,29 %
Pay Out Time before Taxes (POT)b = 2,49 tahun
Pay Out Time after Taxes (POT)a = 2,93 tahun
Return on Investment before Taxes (ROI)b = 25,62 %
Return on Investment after Taxes (ROI)a = 20,49 %
Discounted Cash Flow (DCF) = 16,379%
Shut Down Point (SDP) = 27,44 %
Mempertimbangkan paparan di atas, sudah selayaknya pendirian pabrik
Maleic anhydride ini dikaji lebih lanjut, karena merupakan pabrik yang
menguntungkan dan mempunyai masa depan yang baik.
Maleic Anhydride plant produced by reacting benzene dan oxygen was
plan to be in industrial plant in the region of Cilacap, in Central Java Province.
Plant was established by considering the availability of raw materials,
transportation facilities, readily available labor and environmental conditions.
Plant's production capacity is planned 20,000 tons / year, with operating
time of 24 hours / day and 330 working days in a year. The raw materials used
are much n-butana 2.116,50 kg / hr and Vanadium phosphorus oxcide as
29.186,5629 kg / hr.
Provision of utility plant needs a treatment system and water supply, steam
supply systems, instrument air supply systems, and power generation systems.
Labor needed as many as 137 people with a business entity form Limited
Liability Company (PT) which is headed by a Director who is assisted by the
Director of Production and Director of Finance with line and staff organizational
structure.
From the economic analysis is obtained:
Fixed Capital Investment (FCI) = Rp 440.396.823.280,-
Working Capital Investment (WCI) = Rp 77.717.086.461,-
Total Capital Investment (TCI) = Rp 518.113,909.742,-
Break Even Point (BEP) = 50,29 %
Pay Out Time before Taxes (POT)b = 2,49 tahun
Pay Out Time after Taxes (POT)a = 2,93 tahun
Return on Investment before Taxes (ROI)b = 25,62 %
Return on Investment after Taxes (ROI)a = 20,49 %
Discounted Cash Flow (DCF) = 16,379%
Shut Down Point (SDP) = 27,44 %
Consider the summary above, it is proper establishment of Maleic
anhydride plant to studied further, because the plant is profitable and has good
prospects.
PB  - FAKULTAS TEKNIK
TI  - PRARANCANGAN PABRIK MALEIC ANHYDRIDE
DARI OKSIDASI N-BUTANA OLEH UDARA
KAPASITAS 20.000 TON/TAHUN
(Perancangan Reaktor ( RE-201))
AV  - restricted
ER  -