PRARANCANGAN PABRIK DIETIL MALONAT DARI ASAM MONOKHLOR ASETAT KAPASITAS 12.000 TON / TAHUN
Diethyl malonate plant from monochloracetic acid design with a production capacity of 12,000 tons / year. Diethyl malonate is really needed as raw material in many industry, especially in medical, vitamin and pharmacy industry. Manufacturing process with the following steps: dissolution of raw mater...
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| Main Authors: | , |
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| Format: | Theses and Dissertations NonPeerReviewed |
| Published: |
[Yogyakarta] : Universitas Gadjah Mada
2014
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| Subjects: | |
| Online Access: | https://repository.ugm.ac.id/127940/ http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=68257 |
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| Institution: | Universitas Gadjah Mada |
| Summary: | Diethyl malonate plant from monochloracetic acid design with a production capacity of
12,000 tons / year. Diethyl malonate is really needed as raw material in many industry,
especially in medical, vitamin and pharmacy industry.
Manufacturing process with the following steps: dissolution of raw materials, salt
formation, sianifikasi reaction, the esterification reaction and product separation and
purification processes in the form of decantation process and distillation process.
The plant will be established in Gresik, East Java with a land area of 4 hectares. To
product diethyl malonate with the capacity 12,000 tons/ year, the materials needed are
monochloracetic acid as much as 8723.4 tons/ year, NaOH 40 % as much as 9229.92 tons/ year,
NaCN as much as 4526.52 tons/ year, ethanol 95 % as much as 8940.48 tons/year, H2SO4 98 %
as much as 8310.248 tons/year and benzene as much as 217.08 tons/year. Beside that, to support
this process, the utility takes water as much as 80615.262 M
3
/ year, 868.81 kVA electrical
needs, and steams 351.301 kgs / hour.
Fixed capital required amounted to US$ 60,894,445 + Rp. 126,574,858,327 and working
capital US$ 13,686,946 + Rp 19,942,836,010. Profit before tax is Rp. 10,469,379. And profit
after tax is Rp. 5,234,689. From the results of calculations, the Return on Investment (ROI)
before taxes 31,77 % and 15,88 % after tax. Pay Out Time (POT) before taxes 2,4 years, 3,86
years after tax. Break Even Point 40,70%, Shut Down Point 16,4% and Discounted Cash Flow
Rate Of Return 31,38%. From the results of the feasibility study plants through economic
evaluations have been done on plant diethyl malonate from monochloracetic acid with a
production capacity of 12,000 tons / year can be concluded that the plant deserves to be studied
further. |
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