<> "The repository administrator has not yet configured an RDF license."^^ . <> . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301)"^^ . "Prarancangan Pabrik Monobasic Potassium Phosphate berbahan baku Asam Fosfat dan\r\nPotassium Hidroksida, akan didirikan di Surabaya, Jawa Timur. Pendirian pabrik ini\r\nberdasarkan atas pertimbangan ketersediaan bahan baku, daerah pemasaran, sarana\r\ntransportasi yang memadai, tenaga kerja yang mudah didapatkan dan kondisi\r\nlingkungan yang strategis. Pabrik direncanakan memproduksi Monobasic Potassium\r\nPhosphate sebanyak 30.000 ton/tahun, dengan waktu operasi 24 jam/hari, 330\r\nhari/tahun. Bahan baku yang digunakan adalah Asam Fosfat sebanyak 2.755,322\r\nkg/jam dan Potassium Hidroksida sebanyak 1577,281 kg/jam. Penyediaan kebutuhan\r\nutilitas pabrik Monobasic Potassium Phosphate berupa pengadaan air, pengadaan\r\nlistrik, kebutuhan bahan bakar, pengadaan udara kering dan pengadaan udara\r\ninstrumentasi.\r\nBentuk perusahaan adalah Perseroan Terbatas (PT) menggunakan struktur organisasi\r\nline dan staff dengan jumlah karyawan sebanyak 179 orang.\r\nDari analisis ekonomi diperoleh:\r\nFixed Capital Investment (FCI) = Rp 624.672.379.569,516\r\nWorking Capital Investment (WCI) = Rp 110.236.302.276,973\r\nTotal Capital Investment (TCI) = Rp 734.908.681.846,490\r\nBreak Even Point (BEP) = 41 %\r\nShut Down Point (SDP) = 27 %\r\nPay Out Time before taxes (POT)b = 1,62 tahun\r\nPay Out Time after taxes (POT)a = 1,95 tahun\r\nReturn on Investment before taxes (ROI)b = 44 %\r\nReturn on Investment after taxes (ROI)a = 35 %\r\nDiscounted cash flow (DCF) = 58,02 %\r\nMempertimbangkan paparan di atas, sudah selayaknya pendirian pabrik Monobasic\r\nPotassium Phosphate ini dikaji lebih lanjut, karena merupakan pabrik yang\r\nmenguntungkan dan mempunyai masa depan yang baik.\r\n\r\nDesign of Monobasic Potassium Phosphate plant made from Phosporic Acid and\r\nPotassium Hidroxide, is planned to be established in Surabaya, Jawa Timur. The\r\nestablishment of the factory is based on consideration of the availability of raw\r\nmaterials, process support units, adequate transportation, easily available labor, and\r\nstrategic environmental conditions. The plant is planned to produce 30,000 tons of\r\nMonobasic Potassium Phosphate/year, with an operating time of 24 hours/day, for 300\r\ndays/year. The raw material used is Phosporic Acid as much as 2.755,322 kg/hour and\r\nPotassium Hidroxide as much as 1577,281 kg/hour. The provision of factory utility\r\nneeds consists of water supply units, air supply, electricity supply units, and sewage\r\ntreatment units.\r\nThe form of the company is a Limited Liability Company (Ltd) using a line and staff\r\ncompany organizational structure with a total of 179 workers.\r\nFrom economic analysis, it is obtained that:\r\nFixed Capital Investment (FCI) = Rp 624.672.379.569,516\r\nWorking Capital Investment (WCI) = Rp 110.236.302.276,973\r\nTotal Capital Investment (TCI) = Rp 734.908.681.846,490\r\nBreak Even Point (BEP) = 41 %\r\nShut Down Point (SDP) = 27 %\r\nPay Out Time before taxes (POT)b = 1,62 years\r\nPay Out Time after taxes (POT)a = 1,95 years\r\nReturn on Investment before taxes (ROI)b = 44 %\r\nReturn on Investment after taxes (ROI)a = 35 %\r\nDiscounted cash flow (DCF) = 58,02 %\r\nConsidering the explanation above, it is appropriate for the establishment of a\r\nMonobasic Potassium Phosphate plant to be studied further, because it has high profits\r\nin the future."^^ . "2024-04-05" . . . . . "FAKULTAS TEKNIK"^^ . . . . . . . "Muna Azzahra Pradanta\t"^^ . "Faiz "^^ . "Muna Azzahra Pradanta\t Faiz "^^ . . . . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (File PDF)"^^ . . . "ABSTRAK - Faiz Muna Azzahra Pradanta.pdf"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (File PDF)"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (File PDF)"^^ . . . "FILE TUGAS AKHIR TANPA PEMBAHASAN - Faiz Muna Azzahra Pradanta.pdf"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "indexcodes.txt"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "indexcodes.txt"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "lightbox.jpg"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "preview.jpg"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "medium.jpg"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "small.jpg"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "lightbox.jpg"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "preview.jpg"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "medium.jpg"^^ . . . "PRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI\r\n\r\nASAM FOSFAT DAN POTASSIUM HIDROKSIDA\r\nKAPASITAS 30.000 TON/TAHUN\r\n(Tugas Khusus Perancangan Cooling Tank (CT-301) (Other)"^^ . . . . . . "small.jpg"^^ . . "HTML Summary of #85559 \n\nPRARANCANGAN PABRIK MONOBASIC POTASSIUM PHOSPHATE DARI \n \nASAM FOSFAT DAN POTASSIUM HIDROKSIDA \nKAPASITAS 30.000 TON/TAHUN \n(Tugas Khusus Perancangan Cooling Tank (CT-301)\n\n" . "text/html" . . . "660 Teknik kimia" . .