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PRARANCANGAN PABRIK ISOPROPANOLAMIN DARI PROPILEN OKSIDA DAN AMONIAK KAPASITAS 15.000 TON/TAHUN (Perancangan Menara Distilasi (DC-301))
Pabrik isopropanolamin berbahan baku propilen oksida dan amoniak, akan didirikan di Tanjung Siapi-api, Palembang, Sumatera Selatan. Pabrik ini berdiri dengan mempertimbangkan ketersediaan bahan baku, sarana transportasi yang memadai, tenaga kerja yang mudah didapatkan dan kondisi lingkungan. Pabrik direncanakan memproduksi isopropanolamin sebanyak 15.000 ton/tahun,dengan waktu operasi 24 jam/hari, 330 hari/tahun. Bahan baku yang digunakan adalah propilen oksida sebanyak 1746,11 kg/jam dan amoniak sebanyak 2944,534 kg/jam. Jumlah karyawan sebanyak 143 orang dengan bentuk perusahaan adalah Perseroan Terbatas (PT) menggunakan struktur organisasi line dan staff. Dari analisis ekonomi diperoleh: Fixed Capital Investment (FCI) = Rp 240,590,020,360,- Working Capital Investment (WCI) = Rp 42,457,062,416,- Total Capital Investment (TCI) = Rp 283,047,082,776,- Break Even Point (BEP) = 55% Shut Down Point (SDP) = 25,11% Pay Out Time after Taxes (POT)a = 2,63 tahun Return on Investment after Taxes (ROI)a = 23,75 % Internal Rate Return (IRR) = 29,17% Annual Net Profit (Pa) = Rp 67,247,410,190/tahun Mempertimbangkan paparan di atas, sudah selayaknya pendirian pabrik isopropanolamin ini dikaji lebih lanjut, karena merupakan pabrik yang menguntungkan dan mempunyai masa depan yang baik. A plant to produce isopropanolamine from propylene oxide and ammonia is planned to be located at Tanjung Siapi-Api, Palembang, South Sumatera. The plant is established by considering availability of raw materials, transportation facilities, readily available labor and environmental conditions. Capacity of the plant is 15.000 tons/year operating 24 hour/day and 330 working days/ year. The plant required 1746,11kg/hr propylene oxide and 2944,534 kg/hr ammonia. Quantity of labor is around 143 people. The plant is managed as a Limited Liability Company (PT), which is headed by a Director who is assisted by a Director of Production and Director of Finance. The company is organized in the form of line and staff structure. From analysis of the plant economy is obtained: Fixed Capital Investment (FCI) = Rp 240,590,020,360,- Working Capital Investment (WCI) = Rp 42,457,062,416,- Total Capital Investment (TCI) = Rp 283,047,082,776,- Break Even Point (BEP) = 55% Shut Down Point (SDP) = 25,11% Pay Out Time after Taxes (POT)a = 2,63 year Return on Investment after Taxes (ROI)a = 23,75 % Internal Rate Return (IRR) = 29,17% Annual Net Profit (Pa) = Rp 67,247,410,190/year By considering above the summary, it is suitable study further the isopropanolamine plant since plant is profitable and has good prospects.
PRARANCANGAN PABRIK ISOPROPANOLAMIN DARI PROPILEN OKSIDA DAN AMONIAK KAPASITAS 15.000 TON/TAHUN (Perancangan Menara Distilasi (DC-301)) (File PDF)
PRARANCANGAN PABRIK ISOPROPANOLAMIN DARI PROPILEN OKSIDA DAN AMONIAK KAPASITAS 15.000 TON/TAHUN (Perancangan Menara Distilasi (DC-301)) (Other)
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