PRARANCANGAN PABRIK MONOKLOBENZENE DARI BENZENE DAN KLORIN KAPASITAS 35000 TON/TAHUN
Monochlorobenzene (C6H5Cl) is the result of the chlorination of benzene by reacting chlorine gas and benzene, with the help of a catalyst ferrychloride in bubble stirred reactor at inlet temperature of 80�C and a pressure of 2 atm. The heat of reaction that arises was taken with the cooling water...
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| 格式: | Theses and Dissertations NonPeerReviewed |
| 出版: |
[Yogyakarta] : Universitas Gadjah Mada
2014
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| 主題: | |
| 在線閱讀: | https://repository.ugm.ac.id/131646/ http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=72144 |
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| 總結: | Monochlorobenzene (C6H5Cl) is the result of the chlorination of benzene
by reacting chlorine gas and benzene, with the help of a catalyst ferrychloride in
bubble stirred reactor at inlet temperature of 80�C and a pressure of 2 atm. The heat
of reaction that arises was taken with the cooling water flowing through the coil that
was placed inside reactor. The liquid reaction products that still contain the catalyst is
neutralized in the decanter. Then lighter fluid phase decant distilled to obtain the
results monochlorobenzene out at the top of the tower recycle, while the bottom of the
distillation tower-01 as much as 5163.0398 kg/hour, as much dichlorobenzene
748,8478 kg/hour, and 99% yield of 99% monochlorobenzene out at the top of the
distillation tower-02 at 4419,1919 kg/hour. Hydrochloric acid out of the absorber
5076,9616 kg/hour.
The plant has capacity of 35000 ton/year and is established in
Cilegon,Banten on an area of 6 hectares, including residential and extension. Fixed
capital of Rp243.614.046.621,95 , working capital of Rp 67.917.460.740,79 , percent
return of investment before tax of 33,43% and 16,72% after tax. Break even point is
48.13% and 25.42% shut down point. It can be concluded that this plant is feasible for
further study. |
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