PRARANCANGAN PABRIK SIKLOHEKSANON DARI PHENOL DAN HIDROGEN DENGAN KAPASITAS 41.000 TON/TAHUN Tugas Khusus Perancangan Reaktor (RE-201)
| Main Author: | RENDY PARNINGOTAN PASARIBU, 1315041044 |
|---|---|
| Format: | Bachelors NonPeerReviewed Book Report |
| Terbitan: |
FAKULTAS TEKNIK JURUSAN TEKNIK KIMIA
, 2020
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| Subjects: | |
| Online Access: |
http://digilib.unila.ac.id/65337/1/ABSTRAK.pdf http://digilib.unila.ac.id/65337/2/SKRIPSI%20FULL.pdf http://digilib.unila.ac.id/65337/3/SKRIPSI%20TANPA%20BAB%20PEMBAHASAN.pdf http://digilib.unila.ac.id/65337/ |
Daftar Isi:
- Pabrik sikloheksanon berbahan baku phenol dan hidrogen, akan didirikan di Kabupaten Serang, Banten. Pabrik ini berdiri dengan mempertimbangkan ketersediaan bahan baku, sarana transportasi yang memadai, tenaga kerja yang mudah didapatkan dan kondisi lingkungan. Pabrik direncanakan memproduksi sikloheksanon sebanyak 41.000 ton/tahun, dengan waktu operasi 24 jam/hari, 330 hari/tahun. Bahan baku yang digunakan adalah phenol sebanyak 5.957,392 kg/jam dan hidrogen sebanyak 273,466 kg/jam. Penyediaan kebutuhan utilitas pabrik sikloheksanon 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 177 orang. Dari analisis ekonomi diperoleh: Fixed Capital Investment (FCI) = Rp 701.500.267.666,8460 Working Capital Investment (WCI) = Rp 123.794.164.882,3850 Total Capital Investment (TCI) = Rp 825.294.432.549,2310 Break Even Point (BEP) = 39,7 % Shut Down Point (SDP) = 23,9 % Pay Out Time before taxes Pay Out Time after taxes Return on Investment before taxes (POT)b (POT)a b = = = 1,98 tahun 2,36 tahun after taxes (ROI)a 2347,45 % Discounted cash flow (DCF) = 29,4 % Mempertimbangkan paparan di atas, sudah selayaknya pendirian pabrik sikloheksanon ini dikaji lebih lanjut, karena merupakan pabrik yang menguntungkan dan mempunyai masa depan yang baik. Cyclohexanone plant produced by reacting phenol and hydrogen is planned to be in industrial factory in the region of Serang in Banten Province. Plant will be established by considering the availability of raw materials, transportation facilities, readily available labor and environmental conditions. Production capacity is planned 41,000 tons/year, with operating time of 24 hours/day and 330 working days in a year. The raw materials used are much phenol 5.957,392 kg/hr and hydrogen as 273,466 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 177 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 701.500.267.666,8460 Working Capital Investment (WCI) = Rp 123.794.164.882,3850 Total Capital Investment (TCI) = Rp 825.294.432.549,2310 Break Even Point (BEP) = 39,7 % Shut Down Point (SDP) = 23,9 % Pay Out Time before taxes Pay Out Time after taxes Return on Investment before taxes (POT)b (POT)a b = = = 1,98 years 2,36 years after taxes (ROI)a 2347,45 % Discounted cash flow (DCF) = 29,4 % Consider the summary above,it is proper establishment of cyclohexanone plant to studied further, because the plant is profitable and has good prospects.