Pabrik N-Butanol Dari N-Butiraldehid Dan Hidrogen Dengan Proses Hidrogenasi Kapasitas 60.000 Ton/Tahun

Azzahiro, Tasya Alya (2026) Pabrik N-Butanol Dari N-Butiraldehid Dan Hidrogen Dengan Proses Hidrogenasi Kapasitas 60.000 Ton/Tahun. Undergraduate thesis, UPN Veteran Jawa Timur.

[img] Text (Cover)
22031010016-Cover (2) .pdf

Download (2MB)
[img] Text (Bab 1)
22031010016-Bab 1 (2).pdf

Download (790kB)
[img] Text (Bab 2)
22031010016-Bab 2 (2).pdf

Download (836kB)
[img] Text (Bab 3)
22031010016-Bab 3 .pdf
Restricted to Repository staff only until 26 August 2029.

Download (548kB)
[img] Text (Bab 4)
22031010016-Bab 4 (2).pdf
Restricted to Repository staff only until 26 August 2029.

Download (714kB)
[img] Text (Bab 5)
22031010016-Bab 5 (2).pdf
Restricted to Repository staff only until 26 August 2029.

Download (1MB)
[img] Text (Bab 6)
22031010016-Bab 6.pdf
Restricted to Repository staff only until 26 August 2029.

Download (741kB)
[img] Text (Bab 7)
22031010016-Bab 7 (2) (1).pdf
Restricted to Repository staff only until 26 August 2029.

Download (1MB)
[img] Text (Bab 8)
22031010016-Bab 8.pdf
Restricted to Repository staff only until 26 August 2029.

Download (795kB)
[img] Text (Bab 9)
22031010016-Bab 9 (1).pdf
Restricted to Repository staff only until 26 August 2029.

Download (662kB)
[img] Text (Bab 10)
22031010016-Bab 10 (1).pdf
Restricted to Repository staff only until 26 August 2029.

Download (609kB)
[img] Text (Bab 11)
22031010016-Bab 11.pdf
Restricted to Repository staff only until 26 August 2029.

Download (516kB)
[img] Text (Daftar Pustaka)
22031010016-Daftar pustaka (2).pdf

Download (547kB)
[img] Text (Flowsheet)
22031010016-Flowsheet.pdf

Download (385kB)

Abstract

N-butanol is a chemical widely used as a solvent, chemical industry intermediate, and fuel additive. The increasing demand for n-butanol in Indonesia has prompted the design of an n-butanol plant from n-butyraldehyde and hydrogen through a hydrogenation process with a capacity of 60,000 tons/year. The production process uses a nickel catalyst in two packed bed reactors arranged in series. The first reactor operates at a temperature of 60°C and a pressure of 15 atm, while the second reactor operates at a temperature of 90°C and a pressure of 14 atm. The reaction product is then purified using a distillation process to obtain n-butanol with a purity of 99.9%. The remaining hydrogen and n-butyraldehyde are recycled to increase process efficiency. The plant is planned to be located in the Kotabumi Industrial Estate, Cilegon City, Banten, with an operating time of 330 days/year. Based on the economic analysis, the ROI before tax was 29.50%, ROI after tax was 22.12%, POT was 2 years and 11 months, IRR was 16.56%, and BEP was 32.4%. Based on the results of the technical and economic analysis, the n-butanol plant with a capacity of 60,000 tons/year was deemed feasible to be established.

Item Type: Thesis (Undergraduate)
Contributors:
ContributionContributorsNIDN/NIDKEmail
Thesis advisorKurniati, ElyNIDN0718106402elysentot@gmail.com
Subjects: Q Science > QD Chemistry
Divisions: Faculty of Engineering > Departement of Chemical Engineering
Depositing User: Tasya Alya Azzahiro
Date Deposited: 28 Aug 2026 02:58
Last Modified: 28 Aug 2026 03:49
URI: https://repository.upnjatim.ac.id/id/eprint/58886

Actions (login required)

View Item View Item