<> <http://www.w3.org/2000/01/rdf-schema#comment> "The repository administrator has not yet configured an RDF license."^^<http://www.w3.org/2001/XMLSchema#string> .
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<http://digilib.unila.ac.id/id/eprint/87083> <http://purl.org/dc/terms/title> "PRARANCANGAN PABRIK DIETYL ETHER dari ETHANOL DENGAN\r\nPROSES DEHIDRAS KATALIS ALUMINA DENGAN KAPASITAS 20.000\r\n\r\nTON/TAHUN\r\n\r\n(TUGAS KHUSUS PERANCANGAN REAKTOR (RE-201))"^^<http://www.w3.org/2001/XMLSchema#string> .
<http://digilib.unila.ac.id/id/eprint/87083> <http://purl.org/ontology/bibo/abstract> "Dietil eter merupakan zat kimia DEE banyak digunakan sebagai bahan pelarut untuk\r\nmelakukan reaksi-reaksi organik dan memisahkan senyawa organik. DEE memiliki\r\nnilai ekonomis yang tinggi karena banyak digunakan sebagai pelarut untuk reaksi-reaksi\r\norganik dan mulai dikembangkan untuk bahan bakar alternative. Diethyl ether\r\ndidapatkan oleh reaksi dehidrasi etanol dengan menggunakan katalis asam kuat atau\r\nalumina. Penyediaan kebutuhan Dietil Eter dalam negeri masih sepenuhnya diperoleh dari\r\nimpor, sehingga peluang untuk didirikanya pabrik Dietil Eter memiliki prospek yang bagus.\r\nPenyediaan utilitas pabrik berupa sistem pengolahan dan penyediaan air, sistem refrigerasi,\r\nserta penyedia udara dan instrumentasi. Kapasitas produksi pabrik nitrogliserin\r\ndirencanakan sebesar 20.000 ton/tahun dengan 330 hari kerja dalam 1 tahun. Lokasi pabrik\r\nDEE direncanakan akan didirikan di Jl. Raya Manyar, Manyarejo, Kecamatan\r\nManyar, Kabupaten Gresik, Jawa Timur. Tenaga kerja yang dibutuhkan sebanyak 158\r\norang dengan bentuk badan usaha Perseroan Terbatas (PT) dengan struktur organisasi lini.\r\nDari analisis ekonomi diperoleh:\r\nFixed Capital Investment (FCI) = Rp 1.051.787.973.142\r\nWorking Capital Investment (WCI) = Rp 158.609.642.319\r\nTotal Capital Investment (TCI) = Rp 1.273.397.615.462\r\nTotal Production Cost (TPC) = Rp 3.257.867.492.703\r\nBreak Even Point (BEP) = 39,5%\r\nShut Down Point (SDP) = 28,5%\r\nPay Out Time before taxes (POT)b = 2,2 tahun\r\nPay Out Time after taxes (POT)a = 1,482 tahun\r\nReturn on Investment before taxes (ROI)b = 60,6%\r\nReturn on Investment after taxes (ROI)a = 58%\r\nDiscounted cash flow (DCF) = 57,55%\r\nBerdasarkan hasil analisis diatas, maka pendirian pabrik propilen oksida ini layak untuk\r\ndikaji lebih lanjut, karena merupakan pabrik yang menguntungkan dari sisi ekonomi dan\r\nmempunyai prospek yang relatif baik.\r\nDiethyl ether is a DEE chemical substance widely used as a solvent to carry out\r\norganic reactions and separate organic compounds. DEE has high economic value\r\nbecause it is widely used as a solvent for organic reactions and is starting to be\r\ndeveloped as an alternative fuel. Diethyl ether is obtained by the ethanol\r\ndehydration reaction using a strong acid or alumina catalyst. The supply of domestic\r\nDiethyl Ether needs is still entirely obtained from imports, so the opportunity to\r\nestablish a Diethyl Ether factory has good prospects. Provision of factory utilities\r\nin the form of water processing and supply systems, refrigeration systems, as well\r\nas air and instrumentation supplies. The production capacity of the nitroglycerin\r\nfactory is planned at 20,000 tons/year with 330 working days in 1 year. The DEE\r\nfactory location is planned to be established on Jl. Raya Manyar, Manyarejo,\r\nManyar District, Gresik Regency, East Java. The workforce required is 158 people\r\nin the form of a Limited Liability Company (PT) with a line organizational\r\nstructure.\r\n\r\nAnalysis economic obtained:\r\nFixed Capital Investment (FCI) = Rp 1.051.787.973.142\r\nWorking Capital Investment (WCI) = Rp 158.609.642.319\r\nTotal Capital Investment (TCI) = Rp 1.273.397.615.462\r\nTotal Production Cost (TPC) = Rp 3.257.867.492.703\r\nBreak Even Point (BEP) = 39,5%\r\nShut Down Point (SDP) = 28,5%Pay Out Time before taxes (POT)b = 2,2 tahun\r\nPay Out Time after taxes (POT)a = 1,482 tahun\r\nReturn on Investment before taxes (ROI)b = 60,6%\r\nReturn on Investment after taxes (ROI)a = 58%\r\nDiscounted cash flow (DCF) = 57,55%\r\nBased on the result of the analysis above, the establishment of this propylene oxide\r\nfactory is worthy of further study, because it is a factory that is profitable from an\r\neconomic perspective and has relatively good prospects."^^<http://www.w3.org/2001/XMLSchema#string> .
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<http://digilib.unila.ac.id/id/eprint/87083> <http://eprints.org/ontology/hasDocument> <http://digilib.unila.ac.id/id/document/2373556> .
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<http://digilib.unila.ac.id/id/document/2373556> <http://eprints.org/relation/isVersionOf> <http://digilib.unila.ac.id/id/document/2373513> .
<http://digilib.unila.ac.id/id/document/2373556> <http://eprints.org/relation/isVolatileVersionOf> <http://digilib.unila.ac.id/id/document/2373513> .
<http://digilib.unila.ac.id/id/document/2373556> <http://eprints.org/relation/issmallThumbnailVersionOf> <http://digilib.unila.ac.id/id/document/2373513> .
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<http://digilib.unila.ac.id/id/document/2373556> <http://purl.org/dc/terms/hasPart> <http://digilib.unila.ac.id/87083/10/small.jpg> .
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<http://digilib.unila.ac.id/id/document/2373557> <http://eprints.org/relation/isVolatileVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
<http://digilib.unila.ac.id/id/document/2373557> <http://eprints.org/relation/islightboxThumbnailVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
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<http://digilib.unila.ac.id/id/document/2373558> <http://eprints.org/relation/isVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
<http://digilib.unila.ac.id/id/document/2373558> <http://eprints.org/relation/isVolatileVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
<http://digilib.unila.ac.id/id/document/2373558> <http://eprints.org/relation/ispreviewThumbnailVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
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<http://digilib.unila.ac.id/id/document/2373559> <http://eprints.org/relation/isVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
<http://digilib.unila.ac.id/id/document/2373559> <http://eprints.org/relation/isVolatileVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
<http://digilib.unila.ac.id/id/document/2373559> <http://eprints.org/relation/ismediumThumbnailVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
<http://digilib.unila.ac.id/id/eprint/87083> <http://eprints.org/ontology/hasDocument> <http://digilib.unila.ac.id/id/document/2373560> .
<http://digilib.unila.ac.id/id/document/2373560> <http://www.w3.org/1999/02/22-rdf-syntax-ns#type> <http://eprints.org/ontology/Document> .
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<http://digilib.unila.ac.id/id/document/2373560> <http://eprints.org/relation/isVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
<http://digilib.unila.ac.id/id/document/2373560> <http://eprints.org/relation/isVolatileVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
<http://digilib.unila.ac.id/id/document/2373560> <http://eprints.org/relation/issmallThumbnailVersionOf> <http://digilib.unila.ac.id/id/document/2373512> .
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<http://digilib.unila.ac.id/id/document/2373563> <http://purl.org/dc/terms/hasPart> <http://digilib.unila.ac.id/87083/17/medium.jpg> .
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<http://digilib.unila.ac.id/id/document/2373564> <http://eprints.org/relation/isVolatileVersionOf> <http://digilib.unila.ac.id/id/document/2373511> .
<http://digilib.unila.ac.id/id/document/2373564> <http://eprints.org/relation/issmallThumbnailVersionOf> <http://digilib.unila.ac.id/id/document/2373511> .
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<http://digilib.unila.ac.id/id/document/2373564> <http://purl.org/dc/terms/hasPart> <http://digilib.unila.ac.id/87083/18/small.jpg> .
<http://digilib.unila.ac.id/87083/18/small.jpg> <http://www.w3.org/2000/01/rdf-schema#label> "small.jpg"^^<http://www.w3.org/2001/XMLSchema#string> .
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<http://digilib.unila.ac.id/87083/> <http://purl.org/dc/elements/1.1/format> "text/html" .
<http://digilib.unila.ac.id/87083/> <http://xmlns.com/foaf/0.1/primaryTopic> <http://digilib.unila.ac.id/id/eprint/87083> .
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<http://digilib.unila.ac.id/id/eprint/87083> <http://purl.org/dc/terms/subject> <http://digilib.unila.ac.id/id/subject/620> .
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<http://digilib.unila.ac.id/id/subject/660> <http://www.w3.org/2004/02/skos/core#prefLabel> "660 Teknik kimia" .
<http://digilib.unila.ac.id/id/eprint/87083> <http://purl.org/dc/terms/subject> <http://digilib.unila.ac.id/id/subject/660> .