RAYSA ANINDYA, 0815041050 (2015) PRARANCANGAN PABRIK MAGNESIUM KLORIDA DARI MAGNESIUM HIDROKSIDA DAN ASAM KLORIDA KAPASITAS 35000 TON/TAHUN (PERANCANGAN REAKTOR (R-201). FAKULTAS TEKNIK, UNIVERSITAS LAMPUNG.
|
File PDF
ABSTRACT.pdf Download (7Kb) | Preview |
|
|
File PDF
ABSTRAK.pdf Download (82Kb) | Preview |
|
|
File PDF
COVER DALAM.pdf Download (8Kb) | Preview |
|
|
File PDF
COVER LUAR.pdf Download (10Kb) | Preview |
|
|
File PDF
DAFTAR GAMBAR.pdf Download (4Kb) | Preview |
|
|
File PDF
DAFTAR TABEL.pdf Download (85Kb) | Preview |
|
|
File PDF
LEMBAR PENGESAHAN.pdf Download (122Kb) | Preview |
|
|
File PDF
LEMBAR PERNYATAAN.pdf Download (120Kb) | Preview |
|
|
File PDF
LEMBAR PERSETUJUAN.pdf Download (125Kb) | Preview |
|
|
File PDF
MOTO.pdf Download (104Kb) | Preview |
|
|
File PDF
PERSEMBAHAN.pdf Download (24Kb) | Preview |
|
|
File PDF
RIWAYAT HIDUP.pdf Download (77Kb) | Preview |
|
|
File PDF
SANWACANA.pdf Download (78Kb) | Preview |
|
|
File PDF
SURAT PERNYATAAN BERJILBAB.pdf Download (4Kb) | Preview |
|
|
File PDF
DAFTAR ISI.pdf Download (12Kb) | Preview |
|
|
File PDF
BAB I.pdf Download (242Kb) | Preview |
|
|
File PDF
BAB II.pdf Download (363Kb) | Preview |
|
|
File PDF
BAB III.pdf Download (156Kb) | Preview |
|
![[img]](http://digilib.unila.ac.id/style/images/fileicons/text.png) |
File PDF
BAB IV.pdf Restricted to Hanya pengguna terdaftar Download (248Kb) |
|
|
File PDF
BAB V.pdf Restricted to Hanya pengguna terdaftar Download (372Kb) |
|
|
File PDF
BAB VI.pdf Restricted to Hanya pengguna terdaftar Download (168Kb) |
|
|
File PDF
BAB VII.pdf Restricted to Hanya pengguna terdaftar Download (86Kb) |
|
|
File PDF
BAB VIII.pdf Restricted to Hanya pengguna terdaftar Download (148Kb) |
|
|
File PDF
BAB IX.pdf Restricted to Hanya pengguna terdaftar Download (201Kb) |
|
|
File PDF
BAB X.pdf Restricted to Hanya pengguna terdaftar Download (6Kb) |
|
|
File PDF
DAFTAR PUSTAKA.pdf Download (129Kb) | Preview |
Abstrak (Berisi Bastraknya saja, Judul dan Nama Tidak Boleh di Masukan)
ABSTRAK Pabrik magnesium klorida berbahan magnesium hiroksida dan asam klorida, akan didirikan di Purwakarta Jawa Barat. Pabrik ini berdiri dengan mempertimbangkan ketersediaan bahan baku, sarana transportasi yang memadai, tenaga kerja yang mudah didapatkan dan kondisi lingkungan. Pabrik direncanakan memproduksi magnesium klorida sebanyak 35.000 ton/tahun, dengan waktu operasi 24 jam/hari, 330 hari/tahun. Bahan baku yang digunakan adalah magnesium hidroksida sebanyak 2.853,087 kg/jam dan asam klorida 3.571,864 kg/jam. Penyediaan kebutuhan utilitas pabrik magnesium klorida berupa: pengadaan air, pengadaan steam, 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 138 orang. Dari analisis ekonomi diperoleh: Fixed Capital Investment (FCI) = Rp 284.378.913.289,850 Working Capital Investment (WCI) = Rp 50.184.514.109,974 Total Capital Investment (TCI) = Rp 334.563.427.399,824 Break Even Point (BEP ) = 44,86% Shut Down Point (SDP) = 19,56% Pay Out Time after taxes (POT)a = 3,15 years Return on Investment after taxes (ROI)a = 18,52% Internal Rate Return (IRR) = 24,39% Annual Net Profit (Pa) = Rp 61.966.806,175/year Mempertimbangkan paparan di atas, sudah selayaknya pendirian pabrik Magnesium Klorida ini dikaji lebih lanjut, karena merupakan pabrik yang menguntungkan dan mempunyai masa depan yang baik. ABSTRACT A plant to produce magnesium chloride from magnesium hydroxide and hydrochloride acid is planned to be located at Purwakarta, West Java. The plant is established by considering availability of raw materials, transportation facilities, readily available labor and environmental conditions. Capacity of the plant is 35.000 tons/year operating 24 hour/day and 330 working days/ year. The plant required 2.853,087 kg/hr magnesium hydroxide and 3.571,864 kg/hr hydrochloride acid. Quantity of labor is around 138 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 284.378.913.289,850 Working Capital Investment (WCI) = Rp 50.184.514.109,974 Total Capital Investment (TCI) = Rp 334.563.427.399,824 Break Even Point (BEP) = 44,86% Shut Down Point (SDP) = 19,56% Pay Out Time after Taxes (POT)a = 3,15 year Return on Investment after Taxes (ROI)a = 18,52 % Internal Rate Return (IRR) = 24,39% Annual Net Profit (Pa) = Rp 61.966.806,175/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: | 8094498 . Digilib |
| Date Deposited: | 30 Apr 2015 06:37 |
| Terakhir diubah: | 30 Apr 2015 06:37 |
| URI: | http://digilib.unila.ac.id/id/eprint/9547 |
Actions (login required)
 |
Lihat Karya Akhir |
