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<http://digilib.unila.ac.id/id/eprint/56598> <http://purl.org/dc/terms/title> "MANUFACTURING OF DIMETILETER (C2H6O) FROM METANOL \r\n(CH3COOH) WITH CAPACITY 15.000 TONS/YEAR\r\nDesign of Reactor (RE-201)"^^<http://www.w3.org/2001/XMLSchema#string> .
<http://digilib.unila.ac.id/id/eprint/56598> <http://purl.org/ontology/bibo/abstract> "Dimetil eter (DME) is one of the chemical industry products used as raw material \r\nfor chemical industry, explosive dimetil sulfat ((CH3)2SO4), dimetil sulfit \r\n(C2H6S), asam asetat (CH3COOH) dan formaldehid (CH2O). On the \r\nManufacturing of Dimetil eter was selected direct synthesis process that is more \r\nprofitable in terms of economics and thermodynamics than other processes.\r\nThis Plant is meant to produce 15.000 tons/year with operation time 24 hours/day \r\nand 330 days on a year. This Plant is planned to be built in Batakan, Kalimantan \r\nTimur. The bussines entity form of this plant is Limited Liability Company (Ltd) \r\nusing line and staff organizational structure with 177 labors.\r\nFrom the economic analysis, it is obtained that : \r\nFixed Capital Investment (FCI) = Rp 211.595.041.983,1770 \r\nWorking Capital Investment (WCI) = Rp 39.829.654.961,5391 \r\nTotal Capital Investment (TCI) = Rp 251.424.696.944,7160 \r\nBreak Even Point (BEP) = 44,34%\r\nPay Out Time before taxes (POT)b = 2,11 years\r\nPay Out Time after taxes (POT)a = 2,51 years\r\nRate on investment after taxes (ROI)a = 25,11%\r\nDiscounted Cash Flow (DCF) = 25,44%\r\nShut Down Point (SDP) = 21,02%\r\nConsider the summary above, it is proper establishment of Dimetil eter Plant is\r\nstudied further, because the plant is profitable and has good prospects"^^<http://www.w3.org/2001/XMLSchema#string> .
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