Alvita , Fiksi Azzahra (2024) PRARANCANGAN PABRIK KLORIN DIOKSIDA DARI HIDROGEN PEROKSIDA, NATRIUM KLORAT, DAN ASAM SULFAT DENGAN KAPASITAS 30.000 TON/TAHUN (Perancangan Absorber 301 (AB-301)). FAKULTAS TEKNIK, UNIVERSITAS LAMPUNG.
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Abstrak (Berisi Bastraknya saja, Judul dan Nama Tidak Boleh di Masukan)
Klorin dioksida merupakan senyawa anorganik yang digunakan sebagai bleaching agent dalam industri pulp, kertas dan tekstil menggantikan Cl2, chloride, dan hypocloride. Klorin dioksdia dapat diproduksi dengan beberapa cara antara lain: 1) Proses Solvay 2) Proses Mathiesson dan 3) Proses Hydrogen Peroxide-Atmosphere. Penyediaan kebutuhan utilitas pabrik berupa sistem pengolahan dan penyediaan air, sistem penyediaan steam, cooling water, penyediaan udara, dan instrumentasi. Kapasitas produksi pabrik klorin dioksida direncanakan sebesar 30.000 ton/tahun dengan 330 hari kerja dalam 1 tahun. Lokasi pabrik direncanakan didirikan di Karawang, Jawa Barat. Tenaga kerja yang dibutuhkan sebanyak 108 orang dengan bentuk badan usaha Perseroan Terbatas (PT) dengan struktur organisasi lini. Dari analisis ekonomi diperoleh: Fixed Capital Investment (FCI) = Rp 747.068.700.148 Working Capital Investment (WCI) = Rp 131.835.652.967 Total Capital Investment (TCI) = Rp 878.904.353.115 Break Even Point (BEP) = 48,96% Shut Down Point (SDP) = 22,90% Pay Out Time before taxes (POT)b = 3,82 tahun Pay Out Time after taxes (POT)a = 4,36 tahun Return on Investment before taxes (ROI)b = 21,18% Return on Investment after taxes (ROI)a = 16,94% Discounted cash flow (DCF) = 22,56% Berdasarkan beberapa paparan di atas, maka pendirian pabrik klorin dioksida ini layak untuk dikaji lebih lanjut, karena merupakan pabrik yang menguntungkan dari sisi ekonomi dan mempunyai prospek yang relatif baik. Chlorine dioxide is an organic compound that is used as a bleaching agent in the pulp, paper and textile industries to replace Cl2, chloride, and hypochloride. Chlorine dioxide can be produced in several ways, including: 1) Solvay Process 2) Mathiesson Process and 3) Hydrogen Peroxide-Atmosphere Process. Provision of utility plant needs a treatment system and water supply, steam supply system, cooling water, air, and instrumentation providers. Capacity of the plant is planned to production chlorine dioxide is 30.000 tons/year with 330 working days in a year. The location of plant is planned in Karawang, West Java. Labor needed in this plant as many as 108 people with a business entity form Limited Liability Company (PT) with line organizational structure. From the economic analysis are obtained : Fixed Capital Investment (FCI) = Rp 747.068.700.148 Working Capital Investment (WCI) = Rp 131.835.652.967 Total Capital Investment (TCI) = Rp 878.904.353.115 Break Even Point (BEP) = 48,96% Shut Down Point (SDP) = 22,90% Pay Out Time before taxes (POT)b = 3,82 tahun Pay Out Time after taxes (POT)a = 4,36 tahun Return on Investment before taxes (ROI)b = 21,18% Return on Investment after taxes (ROI)a = 16,94% Discounted cash flow (DCF) = 22,56% By considering above the summary, it is proper establishment of chlorine dioxide plant for studied further, because the plant is profitable and has good prospects future.
| Jenis Karya Akhir: | Skripsi |
|---|---|
| Subyek: | 600 Teknologi (ilmu terapan) > 620 Ilmu teknik dan ilmu yang berkaitan |
| Program Studi: | Fakultas Teknik > Prodi S1-Teknik Kimia |
| Pengguna Deposit: | UPT . Siswanti |
| Date Deposited: | 05 Mar 2025 07:33 |
| Terakhir diubah: | 05 Mar 2025 07:33 |
| URI: | http://digilib.unila.ac.id/id/eprint/85499 |
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