Pra Rancangan Pabrik Etil Asetat Dari Etil Alkohol Dan Asam Asetat Dengan Proses Esterifikasi

Yulia S., Putri Arysanti (2025) Pra Rancangan Pabrik Etil Asetat Dari Etil Alkohol Dan Asam Asetat Dengan Proses Esterifikasi. Undergraduate thesis, UPN Veteran Jawa Timur.

[img] Text (Cover)
21031010128.-cover.pdf

Download (4MB)
[img] Text (Bab 1)
21031010128.-bab1.pdf

Download (410kB)
[img] Text (Bab 2)
21031010128.-bab2.pdf

Download (477kB)
[img] Text (Bab 3)
21031010128.-bab3.pdf
Restricted to Repository staff only until 22 July 2028.

Download (268kB)
[img] Text (Bab 4)
21031010128.-bab4.pdf
Restricted to Repository staff only until 22 July 2028.

Download (280kB)
[img] Text (Bab 5)
21031010128.-bab5.pdf
Restricted to Repository staff only until 22 July 2028.

Download (379kB)
[img] Text (Bab 6)
21031010128.-bab6.pdf
Restricted to Repository staff only until 22 July 2028.

Download (301kB)
[img] Text (Bab 7)
21031010128.-bab7.pdf
Restricted to Repository staff only until 22 July 2028.

Download (2MB)
[img] Text (Bab 8)
21031010128.-bab8.pdf
Restricted to Repository staff only until 22 July 2028.

Download (417kB)
[img] Text (Bab 9)
21031010128.-bab9.pdf
Restricted to Repository staff only until 22 July 2028.

Download (322kB)
[img] Text (Bab 10)
21031010128.-bab10.pdf
Restricted to Repository staff only until 22 July 2028.

Download (1MB)
[img] Text (Bab 11)
21031010128.-bab11.pdf

Download (238kB)
[img] Text (Daftar Pustaka)
21031010128.-daftarpustaka.pdf

Download (226kB)
[img] Text (Lampiran)
21031010128.-lampiran.pdf
Restricted to Repository staff only until 22 July 2028.

Download (4MB)
[img] Text (Flowsheet)
21031010128.-flowsheet.pdf

Download (884kB)

Abstract

An ethyl acetate production plant with a capacity of 60.000 tons per year has been designed utilizing the esterification of ethyl alcohol and acetic acid, employing a heterogeneous catalyst, Amberlite IRC-120 H⁺. This method was selected due to its high conversion efficiency (96%), favorable operating conditions (110°C, 1 atm), and cost-effective operation. The process flow is divided into three key stages: pre-treatment, reaction and separation, and final purification, ultimately producing ethyl acetate with a purity level of 99.9%. The plant requires approximately 3.966 kg/h of ethyl alcohol and 5.278 kg/h of acetic acid as its primary raw materials. It is planned to operate continuously for 330 days annually, situated on a 29.925 m² site, and supported by a workforce of 155 personnel. From an economic perspective, the project demonstrates strong viability, with a fixed capital investment of IDR 580 billion, generating annual sales of IDR 6.51 trillion, and incurring raw material costs of IDR 4.13 trillion per year. The economic indicators include a post-tax ROI of 37.09%, an IRR of 23.30%, a payback period of 2 years, and a break-even point (BEP) at 40.34% of production capacity. The development of this plant is expected to significantly reduce reliance on imported ethyl acetate, fulfill domestic industrial demand, and strengthen the self-sufficiency and growth of Indonesia’s chemical manufacturing sector.

Item Type: Thesis (Undergraduate)
Contributors:
ContributionContributorsNIDN/NIDKEmail
Thesis advisorKurniati, ElyNIDN0718106402UNSPECIFIED
Subjects: T Technology > TP Chemical technology
T Technology > TP Chemical technology > TP155 Chemical engineering
Divisions: Faculty of Engineering > Departement of Chemical Engineering
Depositing User: Putri Arysanti Yulia S.
Date Deposited: 22 Jul 2025 02:46
Last Modified: 22 Jul 2025 02:46
URI: https://repository.upnjatim.ac.id/id/eprint/40103

Actions (login required)

View Item View Item