Nugraha, Hanindya and Gracia, Stella (2024) Pra-Desain Pabrik Surfaktan Metil Ester Sulfonat Dari Crude Palm Oil (CPO). Other thesis, Institut Teknologi Sepuluh Nopember.
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Abstract
Pra Desain Pabrik Surfaktan Metil Ester Sulfonat dari Crude Palm Oil dengan kapasitas 10.000 ton/tahun dilakukan melalui proses pre-treatment, konversi crude palm oil (CPO) menjadi metil ester, dan mengonversi metil ester menjadi metil ester sulfonat (MES). Pabrik ini direncanakan untuk bisa beroperasi dengan jumlah 330 hari per tahun dengan waktu kerja 24 jam/hari. Pabrik ini akan didirikan di Kawasan Industri Gresik yang terletak di Kabupaten Gresik, Jawa Timur. Dengan pendirian pabrik di tempat ini, akan memberikan akses terhadap kebutuhan reagen yang berasal dari PT Petrokimia Gresik. Bahan baku berupa Crude Palm Oil (CPO) didapatkan dari PT Perkebunan Nusantara XIII yang terpusat di Kalimantan. Secara proses, akan dimulai dengan Unit Transesterifikasi, Unit Sulfonasi, dan terakhir Unit Pengeringan. Dalam rencana, pabrik ini akan didirikan selama 2 tahun dengan umur pabrik 10 tahun. Untuk memproduksi 10000 ton/tahun surfaktan MES, dibutuhkan capital expenditure (CAPEX) sebesar Rp 127.944.049.381 dan operating expenditure (OPEX) sebesar Rp 340.210.734.581,23. Sumber dana investasi dari modal sendiri sebesar 60% dan modal pinjaman 40%. Berdasarkan analisa ekonomi yang dilakukan, didapatkan bahwa Internal Rate of Return adalah 33% dengan Net Present Value (NPV) positif sebesar Rp 172.193.849.005. Waktu pengembalian modal dari pabrik selama 3 tahun 2 bulan dengan Break Even Point (BEP) sebesar 28,3%. Dari analisis kelayakan ekonomi ini, didapatkan bahwa pabrik layak untuk didirikan.
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Preliminary Plant Design of Methyl Ester Sulfonate Surfactant from Crude Palm Oil (CPO) is designed with a capacity of 10.000 ton/year. This is carried through a pre-treatment process, conversion of crude palm oil (CPO) to methyl ester and followed by conversion of methyl ester to methyl ester sulfonate. This plant is planned to be operating for 330 days per year. This plant will be built in Kawasan Industri Gresik which is located in Kabupaten Gresik, Jawa Timur. Built in Gresik, this will give and provide an access towards the reagent used taken from PT Petrokimia Gresik. The raw material of Crude Palm Oil (CPO) will be obtained from PT Perkebunan Nusantara XIII based in Kalimantan. In terms of process, it will start from Transesterification Unit, Sulfonation Unit, and lastly the Drying Unit. As a plan, this plant will be built in 2 years with 10 year lasting of factory life. To product 10000 ton/year of MES, capital expenditure (CAPEX) needed is Rp 127.944.049.381 and operating expenditure (OPEX) needed is Rp 340.210.734.581,23. Source of investment funds came from equity for 60% and loan for the other 40%. Based on the economic analysis, the Internal Rate of Return is 33% with a Net Present Value (NPV) positive in Rp 172.193.849.005. The pay-out time needed is 3 years and 2 months with a Break Even Point (BEP) in 28,3%. From the feasibility analysis, concluded that the plant is feasible to establish.
| Item Type: | Thesis (Other) |
|---|---|
| Uncontrolled Keywords: | Surfaktan, Crude Palm Oil, Esterifikasi, Transesterifikasi, Sulfonasi, Surfactant, Esterification, Transesterification, Sulfonation |
| Subjects: | T Technology > TP Chemical technology T Technology > TP Chemical technology > TP994 Surface active agents. |
| Divisions: | Faculty of Industrial Technology and Systems Engineering (INDSYS) > Chemical Engineering > 24201-(S1) Undergraduate Thesis |
| Depositing User: | Hanindya Nugraha |
| Date Deposited: | 19 Jul 2024 06:25 |
| Last Modified: | 19 Jul 2024 06:25 |
| URI: | http://repository.its.ac.id/id/eprint/108507 |
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