<> "The repository administrator has not yet configured an RDF license."^^ . <> . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n "^^ . "Selulosa diasetat merupakan salah satu produk industri kimia yang digunakan\r\nsebagai bahan baku pembuatan membran, filter rokok, textil, dan bio-plastic.\r\nSelulosa diasetat dapat di produksi dengan proses esterifikasi dengan menggunakan\r\nbeberapa katalis yang berbeda yaitu 1) Proses esterifikasi dengan katalis asam\r\nsulfat, dan 2) Proses esterifikasi dengan katalis Natrium Bisulfat. Penyediaan\r\nkebutuhan utilitas pabrik berupa sistem pengolahan dan penyediaan air, sistem\r\npenyediaan Thermal oil, Chills water, sistem penyediaan udara tekan dan proses,\r\ndan sistem pembangkit tenaga listrik. \r\n\r\nKapasitas produksi pabrik direncanakan 24.000 ton/tahun dengan 330 hari kerja\r\ndalam 1 tahun. Lokasi pabrik direncanakan didirikan di daerah Jabung, Jambi.\r\nTenaga kerja yang dibutuhkan sebanyak 160 orang dengan bentuk badan usaha\r\nPerseroan Terbatas (PT) yang dipimpin oleh seorang Direktur Utama yang dibantu\r\noleh Direktur Produksi dan Direktur Keuangan dengan struktur organisasi line and\r\nstaff. \r\n\r\nDari analisis ekonomi diperoleh:\r\nFixed Capital Investment (FCI) = Rp 1.161.316.058.446\r\nWorking Capital Investment (WCI) = Rp 204.938.127.961\r\nTotal Capital Investment (TCI) = Rp 1.366.254.186.407\r\nBreak Even Point (BEP) = 36,1 %\r\nShut Down Point (SDP) = 21,8 %\r\nPay Out Time before taxes (POT)\r\nb \r\n= 1,6 years\r\nPay Out Time after taxes (POT)\r\na \r\n= 1,94 years\r\nReturn on Investment before taxes (ROI)\r\nb\r\n = 44,19%\r\nReturn on Investment after taxes (ROI)\r\na \r\n = 41,49%\r\nDiscounted cash flow (DCF) = 42,94%\r\n \r\nMempertimbangkan rangkuman di atas, sudah selayaknya pendirian pabrik\r\nSelulosa Diasetat ini dikaji lebih lanjut, karena merupakan pabrik yang\r\nmenguntungkan dan mempunyai prospek yang baik.\r\n\r\n\r\nCellulose diacetate is one of chemical industry’s product which used as raw material\r\nfor membrane production, cigarettes filter, textile, and bio-plastic. Cellulose\r\ndiacetate can be made through esterfication process by using some different\r\ncatalysts, that are 1) Esterification process by using sulfuric acid catalyst 2)\r\nEsterification process by using Sodium bisulphate catalyst. The supply of plant\r\nutilities are water supply, thermal oil supply, chilling water, compressed air supply,\r\nand process air supply. \r\n\r\nPlants capacity that had been planned was 24.000 tons/year with 330 working days\r\nin a year. The location of plant construction that had been planned was in Jabung,\r\nJambi. The labours which needed for are about 160, with Perseroan Terbatas (PT)\r\nas the type of bussiness enity headed by Chief Executive Officer and helped by\r\nDirector of Production also Director of Finance with line and staff organization\r\nstructure. \r\n\r\nFrom the economical analysis, these are can be obtained:\r\nFixed Capital Investment (FCI) = Rp 1.161.316.058.446\r\nWorking Capital Investment (WCI) = Rp 204.938.127.961\r\nTotal Capital Investment (TCI) = Rp 1.366.254.186.407\r\nBreak Even Point (BEP) = 36,1 %\r\nShut Down Point (SDP) = 21,8 %\r\nPay Out Time before taxes (POT)\r\nb \r\n= 1,6 years\r\nPay Out Time after taxes (POT)\r\na \r\n= 1,94 years\r\nReturn on Investment before taxes (ROI)\r\nb\r\n = 44,19%\r\nReturn on Investment after taxes (ROI)\r\na \r\n = 41,49%\r\nDiscounted cash flow (DCF) = 42,94%\r\n \r\nBy considering the summaries above, it is better to take proper study of Cellulose\r\nDiacetate Plant establishment, it is because of the profitable and good prospects of\r\nthe plant.\r\n \r\n \r\n "^^ . "2017-01-11" . . . . . "FAKULTAS TEKNIK"^^ . . . . . . . "1115041019"^^ . "Fitriani Wulandari "^^ . "1115041019 Fitriani Wulandari "^^ . . . . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (File PDF)"^^ . . . "2. ABSTRAK (ABSTRACT).pdf"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "lightbox.jpg"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "preview.jpg"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "medium.jpg"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "small.jpg"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "indexcodes.txt"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (File PDF)"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (File PDF)"^^ . . . "SKRIPSI TANPA BAB PEMBAHASAN.pdf"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "lightbox.jpg"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "preview.jpg"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "medium.jpg"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "small.jpg"^^ . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "PRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA\r\nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \r\n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201))\r\n\r\n\r\n \r\nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND\r\nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \r\n(Specialized Assignment of Acetylation Reactor Predesign (RE-201))\r\n \r\n (Other)"^^ . . . . . . "indexcodes.txt"^^ . . "HTML Summary of #25664 \n\nPRARANCANGAN PABRIK SELULOSA DIASETAT DARI SELULOSA \nDAN ASETAT ANHIDRAT DENGAN KAPASITAS 24.000 TON/TAHUN \n(Tugas Khusus Perancangan Reaktor Asetilasi (RE-201)) \n \n \n \nPREDESIGN OF CELLULOSE DIACETATE FROM CELLULOSE AND \nACETATE ANHYDRATE WITH CAPACITY OF 24.000 TONS/YEAR \n(Specialized Assignment of Acetylation Reactor Predesign (RE-201)) \n \n \n\n" . "text/html" . . . "QD Chemistry"@en . . . "Teknologi (General)"@id . .