| dc.description | Factory' of Hydrogen Peroxide from isoprapanol provide a very bright
prospect remembering that Hydrogen Peroxide used much by industries, as
Hvdrogen Peroxide is one of the needs being an aid chemical substances. Reaction
happening in making process of Hydrogen Peroxide from isopropanol taking
place in a gas- liquid phase by using a bubble reactor. The reaction is exothermal
in nature. Reactor operates in temperature 130°C with pressure 1atm.
Factory of Hydrogen Peroxide is designed with capacity 25 000 ton/year
It needs standard materials as much as 4642,. jo'd kg/hour. Utilities needed in the
form of water as much as 9682,4190 kg/hour, 1884,3962 as steam and need of
electric as much as 512,6997 KW. The factory is planned to establish in Cilegon,
Banten having land area 17,810 ha. The factory is planned to operate during 24
hours during 330 days in a year. Working force needed as many as 112 persons.
Fixed capital obtained is US $ 19,538,948,81 for funding production
procurement come from abroad and Rp 37.721.714.867, 52 in procuring
local/domestic prodpction facilities The working capital as much as Rp
169.525.958.489,91. Results of economical evaluation show that profits beforetax
is Rp 95.860.061.426,87/year and after-tax is Rp 57.516.036.856,12/year.
Return On Investment (ROI) before-tax 39,4679% and after-tax 23,6807% Pay
Out Time (POT) before-tax . -, ^- ^ and after-tax 2,3691. year. Discounted Cash
Flow (DCF) as big as 49,188%, Break Event Point (BEP) as big as 43,31%
capacity. Whereas Shut Down Point (SDP) as big as 23,20%. Based on
considerations ofeconomical evaluation results, the factory ofhydrogen peroxide
from isopropanol is reasonable to establish
Pabrik Hidrogen Peroksida dari isopropanol memberikan prospek yang sangat
cerah mengingat Hidrogen Peroksida banyak digunakan di dalam industri, karena
Hidrogen Peroksida merupakan salah satu kebutuhan sebagai bahan kimia pembantu .
Reaksi yang terjadi pada proses pembuatan Hidrogen Peroksida dari isopropanol dari
berlangsung dalam fase gas - cair menggunakan reaktor gelembung. Reaksi itu
bersifat eksotermal. Reaktor bekerja pada suhu 130 °C dan tekanan 1atm.
Pabrik Hidrogen Peroksida dirancang dengan kapasitas 25.000 ton/tahun.
Membutuhkan bahan baku isopropanol sebanyak 4642,008 kg/jam. Utilitas yang
diperlukan berupa air sebanyak 9682,4190 kg/jam, 1884,3962 sebagai steam, dan
kebutuhan listrik sebesar 512,6997 KW. Pabrik direncanakan didirikan di Cilegon,
Banten dengan luas tanah 17,810 ha. Pabrik direncanakan beroperasi selama 24 jam
sehari selama 330 hari dalam setahun. Tenaga kerja yang dibutuhkan sebanyak 112
orang
Modal tetap yang diperoleh sebesar US $ 19,538,984.81 untuk biaya
pengedaan produksi yang berasal dari luar negeri dan Rp. 37.721.714.867,52 untuk
pengedaan fasilitas produksi dalam negeri/local. Modal kerja sebesar Rp.
169.525.958.489,91 Hasil evaluasi ekonomi menunjukan keuntungan sebelum pajak
Rp. 95.860.061.426,87/tahun dan sesudah pajak Rp. 57.516.036.856,12/tahun.
Return On Investnment (ROI) sebelum pajak 39,4679 % dan sesudah pajak 23,6807
%. Pay Out Time (POT) sebelum pajak 2,0215 tahun dan sesudah pajak 2,9691
tahun. Discounted Cash Flow (DCF) sebesar 49,188 %, Break Event Point (BEP)
adalah 43,31 % kapasitas, Sedangkan Shut Down Point (SDP) sebesar 23,20 %.
Berdasarkan pertimbangan hasil evaluasi ekonomi, maka pabrik hidrogen peroksida
dari isopropanol sangat layak didirikan. | en_US |
