Adelina, 0815041017 (2015) PRARANCANGAN PABRIK ISOPROPANOLAMIN DARI PROPILEN OKSIDA DAN AMONIAK KAPASITAS 15.000 TON/TAHUN (Tugas Khusus Reaktor 01 (RE-201). FAKULTAS TEKNIK, UNIVERSITAS LAMPUNG.
|
File PDF
ABSTRACT.pdf Download (8Kb) | Preview |
|
|
File PDF
ABSTRAK.pdf Download (7Kb) | Preview |
|
|
File PDF
COVER DALAM.pdf Download (35Kb) | Preview |
|
|
File PDF
COVER LUAR.pdf Download (35Kb) | Preview |
|
|
File PDF
DAFTAR GAMBAR.pdf Download (8Kb) | Preview |
|
|
File PDF
DAFTAR ISI.pdf Download (12Kb) | Preview |
|
|
File PDF
DAFTAR TABEL.pdf Download (119Kb) | Preview |
|
|
File PDF
HALAMAN PENGESAHAN.pdf Download (116Kb) | Preview |
|
|
File PDF
HALAMAN PERSETUJUAN.pdf Download (116Kb) | Preview |
|
|
File PDF
MOTTO.pdf Download (125Kb) | Preview |
|
|
File PDF
PERNYATAAN.pdf Download (56Kb) | Preview |
|
|
File PDF
PERSEMBAHAN.pdf Download (26Kb) | Preview |
|
|
File PDF
RIWAYAT HIDUP.pdf Download (121Kb) | Preview |
|
|
File PDF
PERSEMBAHAN.pdf Download (26Kb) | Preview |
|
|
File PDF
SANWACANA.pdf Download (94Kb) | Preview |
|
|
File PDF
BAB I.pdf Download (269Kb) | Preview |
|
|
File PDF
BAB II.pdf Download (455Kb) | Preview |
|
|
File PDF
BAB III.pdf Download (192Kb) | Preview |
|
File PDF
BAB IV.pdf Restricted to Hanya pengguna terdaftar Download (245Kb) | Minta salinan |
||
File PDF
BAB V.pdf Restricted to Hanya pengguna terdaftar Download (594Kb) | Minta salinan |
||
File PDF
BAB VI.pdf Restricted to Hanya pengguna terdaftar Download (243Kb) | Minta salinan |
||
File PDF
BAB VII.pdf Restricted to Hanya pengguna terdaftar Download (174Kb) | Minta salinan |
||
File PDF
Bab VIII.pdf Restricted to Hanya pengguna terdaftar Download (301Kb) | Minta salinan |
||
File PDF
BAB IX.pdf Restricted to Hanya pengguna terdaftar Download (293Kb) | Minta salinan |
||
File PDF
Bab X.pdf Restricted to Hanya pengguna terdaftar Download (7Kb) | Minta salinan |
||
|
File PDF
DAFTAR PUSTAKA.pdf Download (177Kb) | Preview |
Abstrak (Berisi Bastraknya saja, Judul dan Nama Tidak Boleh di Masukan)
ABSTRAK 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. ABSTRACT 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 1746,11 kg/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.
Jenis Karya Akhir: | Skripsi |
---|---|
Subyek: | > QD Chemistry |
Program Studi: | Fakultas Teknik > Prodi S1-Teknik Kimia |
Pengguna Deposit: | 4208370 . Digilib |
Date Deposited: | 28 Apr 2015 04:44 |
Terakhir diubah: | 28 Apr 2015 04:44 |
URI: | http://digilib.unila.ac.id/id/eprint/9151 |
Actions (login required)
Lihat Karya Akhir |