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<http://digilib.unila.ac.id/id/eprint/56672> <http://purl.org/dc/terms/title> "PRARANCANGAN PABRIK MAGNESIUM SULFAT \r\nHEPTAHIDRAT DARI MAGNESIUM OKSIDA \r\nDAN ASAM SULFAT KAPASITAS 50.000 TON/TAHUN\r\nTugas Khusus Perancangan Crystallizer 301 (CR-301)\r\n"^^<http://www.w3.org/2001/XMLSchema#string> .
<http://digilib.unila.ac.id/id/eprint/56672> <http://purl.org/ontology/bibo/abstract> "Magnesium sulfat heptahidrat merupakan salah satu hasil industri kimia yang \r\ndibutuhkan baik sebagai bahan tambahan pupuk, bahan untuk obat-obatan, dan bahan \r\nintermediate. Magnesium sulfat heptahidrat dihasilkan dari reaksi antara magnesium \r\noksida dan asam sulfat. Kebutuhan dalam negeri akan magnesium sulfat heptahidrat\r\ndiperkirakan akan meningkat sehingga dibutuhkan pabrik yang mampu memenuhi \r\nkebutuhan dalam negeri. \r\nPabrik magnesium sulfat heptahidrat ini direncanakan akan didirikan di Kawasan \r\nIndustri Cilegon, Jalan Gunung Sugih No. 75, Provinsi Banten. Pabrik ini direncanakan \r\nakan menghasilkan magnesium sulfat heptahidrat sebanyak 50.000 ton/tahun, dengan \r\nwaktu operasi 330 hari/tahun. Bahan baku untuk magnesium oksida diperoleh dari PT. \r\nUNIKEMIKA Asia, Bogor dan asam sulfat yang diperoleh dari PT. Insoclay \r\nAcidatama Indonesia, Tangerang.\r\nTahapan proses pabrik magnesium sulfat heptahidrat ini terdiri dari penyiapan bahan \r\nbaku, tahap reaksi, dan tahap separasi dan pemurnian. Unit utilitas pada pabrik \r\nmagnesium sulfat heptahidrat terdiri atas unit penyedia air, penyedia listrik, penyedia \r\nsteam dan penyedia bahan bakar. \r\nBentuk perusahaan adalah Perseroan Terbatas (PT), menggunakan struktur organisasi \r\nline and staff dengan kebutuhan karyawan 153 orang. Dari hasil evaluasi ekonomi \r\ndiperoleh :\r\nFixed Capital Investment (FCI) = Rp 311.765.214.641\r\nWorking Capital Investment (WCI) = Rp 55.017.390.819\r\nTotal Capital Investment (TCI) = Rp 366.782.605.460\r\nBreak Even Point (BEP) = 38,5268 %\r\nShut Down Point (SDP) = 28,4046 %\r\nPay Out Time after taxes (POT)a = 2,21 tahun\r\nReturn on Investment after taxes (ROI)a = 32,7451 %\r\nDiscounted cash flow (DCF) = 35,30 %\r\nHasil studi kelayakan teknik dan ekonomi menyatakan bahwa pendirian Pabrik \r\nMagnesium Sulfat Heptahidrat layak dikaji lebih lanjut.\r\nKata Kunci : Magnesium sulfat heptahidrat, magnesium oksida, asam sulfat\r\n\r\n\r\nMagnesium sulfate heptahydrate is one of the chemical manufacture products that are \r\nneeded both as fertilizer additives, ingredients for medicines, and intermediate in \r\nindustry materials. Magnesium sulfate heptahydrate is produced from the reaction \r\nbetween magnesium oxide and sulfuric acid. Domestic demand for magnesium sulfate \r\nheptahydrate is expected to increase so that we need factories that can satisfy the \r\ndemand of the product needs.\r\nThe Magnesium Sulfate Heptahydrate Plant is planned to be established in the Cilegon \r\nIndustrial Area, Gunung Sugih Street No. 75, Banten Province. This factory is planned \r\nto produce 50,000 tons of magnesium sulfate heptahydrate, with an operating time of \r\n330 days / year. The raw material for magnesium oxide is obtained from PT. \r\nUNIKEMIKA Asia, Bogor and sulfuric acid obtained from PT. Insoclay Acidatama \r\nIndonesia, Tangerang.\r\nThe stages of the magnesium sulphate heptahydrate manufacturing process consist of \r\npreparation of raw materials, reaction stages, and separation & purification stages. The \r\nsupplies of plant’s utility are: water supply units, electricity, steam and fuel. The\r\ncompany entity form is Limited Liability Company (PT), using a line and staff \r\norganization structure with the labors of 153 people. Plant’s economic evaluation are:\r\nFixed Capital Investment (FCI) = Rp 311.765.214.641\r\nWorking Capital Investment (WCI) = Rp 55.017.390.819\r\nTotal Capital Investment (TCI) = Rp 366.782.605.460\r\nBreak Even Point (BEP) = 38,5268 %\r\nShut Down Point (SDP) = 28,4046 %\r\nPay Out Time after taxes (POT)a = 2,21 years\r\nReturn on Investment after taxes (ROI)a = 32,7451 %\r\nDiscounted cash flow (DCF) = 35,30 %\r\nThe results of technical and economic feasibility study is feasible and need further \r\nanalysis, because the plant is profitable with good sustainability.\r\nKey Word : Magnesium sulfate heptahydrate, magnesium oxide, sulfuric acid."^^<http://www.w3.org/2001/XMLSchema#string> .
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