<> "The repository administrator has not yet configured an RDF license."^^ . <> . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301)"^^ . "\r\n\r\n\r\n\r\n\r\n\r\n\r\n\r\n\r\nABSTRAK\r\n\r\n\r\n\r\n\r\nPRA RANCANGAN PABRIK KALIUM HIDROKSIDA DARI KCL DAN AIR DENGAN PROSES ELEKTROLISIS \r\nKAPASITAS 20.000 TON/ TAHUN\r\n(Perancangan Reaktor Elektrolisis (RE-301)) \r\nOleh\r\n IFFAH FITRIA\r\n\r\n\r\n\r\n\r\nPabrik Kalium hidroksida berbahan baku kalium klorida dan air, akan didirikan di Kebomas, Kediri. Pabrik ini berdiri dengan mempertimbangkan ketersediaan bahan baku, sarana transportasi yang memadai, tenaga kerja yang mudah didapatkan dan kondisi lingkungan.\r\nPabrik direncanakan memproduksi kalium hidroksida sebanyak 20.000 ton/tahun, dengan waktu operasi 24 jam/hari, 330 hari/tahun. Bahan baku yang digunakan adalah kalium klorida sebanyak 3.445,114 kg/jam.\r\nPenyediaan kebutuhan utilitas pabrik ini berupa: pengadaan air, pengadaan steam, pengadaan listrik, kebutuhan bahan bakar, dan pengadaan udara kering.\r\nBentuk perusahaan adalah Perseroan Terbatas (PT) menggunakan struktur organisasi line dan staff dengan jumlah karyawan sebanyak 158 orang.\r\nDari analisis ekonomi diperoleh:\r\nFixed Capital Investment\t(FCI)\t=\tRp 203.591.529.515\r\nWorking Capital Investment\t(WCI)\t=\tRp 35.927.916.973\r\nTotal Capital Investment\t(TCI)\t=\tRp 237.483.531.192\r\nBreak Even Point\t(BEP)\t=\t54,33 %\r\nShut Down Point\t(SDP)\t=\t37,53 %\r\nPay Out Time before taxes\r\nPay Out Time after taxes\r\nReturn on Investment before taxes\t(POT)b\r\n(POT)a\r\n(ROI)b\t=\r\n=\r\n=\t2,32 tahun\r\n2,74 tahun\r\n28,01 %\r\nReturn on Investment after taxes\t(ROI)a\t=\t22,44 %\r\nDiscounted cash flow\t(DCF)\t=\t39,35 %\r\nMempertimbangkan paparan di atas, sudah selayaknya pendirian pabrik ini dikaji lebih lanjut, karena merupakan pabrik yang menguntungkan dan mempunyai masa depan yang baik.\r\n\r\n\r\n\r\n\r\n\r\n\r\nABSTRACT\r\n\r\n\r\n\r\n\r\nMANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS PROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301))\r\n\r\n\r\n\r\n\r\nBy\r\n\r\nIFFAH FITRIA\r\n\r\n\r\n\r\n\r\nPotassium hydroxide plant produced by reacting chloride potassium and water was plan to be in industrial plant in the region of Kebomas in Kediri. Plant was established by considering the availability of raw materials, transportation facilities, readily available labor and environmental conditions.\r\nPlant's production capacity is planned 20,000 tons / year, with operating time of 24 hours / day and 330 working days in a year. The raw materials used are much chloride potassium 3.445,114 kg / hr.\r\nProvision of utility plant needs a treatment system and water supply, steam supply systems, instrument air supply systems, and power generation systems.\r\nLabor needed as many as 158 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.\r\nFrom the economic analysis is obtained:\r\nFixed Capital Investment(FCI)\t=Rp 203.591.529.515\r\nWorking Capital Investment(WCI)\t=Rp 35.927.916.973\r\nTotal Capital Investment(TCI)\t=Rp 237.483.531.192\r\nBreak Even Point(BEP)\t=54,33 %\r\nShut Down Point\t(SDP)\t=37,53 %\r\nPay Out Time before taxes\r\nPay Out Time after taxes\r\nReturn on Investment before taxes(POT)b=2,32 years\r\n(POT)a=2,74 years\r\n(ROI)b=28,01 %\r\nReturn on Investment after taxes(ROI)a\t=22,44 %\r\nDiscounted cash flow\t(DCF)\t=\t39,35 %\r\nConsider the summary above, it is proper establishment of potassium hydroxide plant to studied further, because the plant is profitable and has good prospects.\r\n"^^ . "2016-03-02" . . . . . "Fakultas Teknik"^^ . . . . . . . "0815041040"^^ . "IFFAH FITRIA"^^ . "0815041040 IFFAH FITRIA"^^ . . . . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (File PDF)"^^ . . . "SKRIPSI TANPA BAB PEMBAHASAN.pdf"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "indexcodes.txt"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "lightbox.jpg"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "preview.jpg"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "medium.jpg"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "small.jpg"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (File PDF)"^^ . . . "2. ABSTRAK (ABSTRACT).pdf"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (File PDF)"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "lightbox.jpg"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "preview.jpg"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "medium.jpg"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "small.jpg"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . . "indexcodes.txt"^^ . . . "MANUFACTURE OF POTASSIUM HYDROXIDE\r\nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS\r\nPROCESS CAPACITY 20.000 TONS/YEAR\r\n(Design Electrolysis Reactor (RE-301) (Other)"^^ . . . . . "HTML Summary of #21674 \n\nMANUFACTURE OF POTASSIUM HYDROXIDE \nFROM CHLORIDE POTASSIUM AND WATER WITH ELECTROLYSIS \nPROCESS CAPACITY 20.000 TONS/YEAR \n(Design Electrolysis Reactor (RE-301)\n\n" . "text/html" . . . "QD Chemistry"@en . . . "Teknologi (General)"@id . .