PRA RENCANA PABRIK PEMBUATAN ETILBENZENA DENGAN PROSES OKSIDATIF KOPLING METANA KAPASITAS PRODUKSI 280.000 TON PER TAHUN

RIJAL, IHSANUL and Agustina, Tuty Emilia (2018) PRA RENCANA PABRIK PEMBUATAN ETILBENZENA DENGAN PROSES OKSIDATIF KOPLING METANA KAPASITAS PRODUKSI 280.000 TON PER TAHUN. Undergraduate thesis, Sriwijaya University.

[thumbnail of RAMA_24201_03031181320068.pdf] Text
RAMA_24201_03031181320068.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (1MB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_TURNITIN.pdf] Text
RAMA_24201_03031181320068_TURNITIN.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (196kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_01_Front_Ref.pdf]
Preview
Text
RAMA_24201_03031181320068_0009087208_01_Front_Ref.pdf - Submitted Version
Available under License Creative Commons Public Domain Dedication.

Download (722kB) | Preview
[thumbnail of RAMA_24201_03031181320068_0009087208_02.pdf] Text
RAMA_24201_03031181320068_0009087208_02.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (148kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_03.pdf] Text
RAMA_24201_03031181320068_0009087208_03.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (337kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_04.pdf] Text
RAMA_24201_03031181320068_0009087208_04.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (447kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_05.pdf] Text
RAMA_24201_03031181320068_0009087208_05.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (346kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_07.pdf] Text
RAMA_24201_03031181320068_0009087208_07.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (364kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_06.pdf] Text
RAMA_24201_03031181320068_0009087208_06.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (576kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_08.pdf] Text
RAMA_24201_03031181320068_0009087208_08.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (118kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_09.pdf] Text
RAMA_24201_03031181320068_0009087208_09.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (9kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_10_ref.pdf] Text
RAMA_24201_03031181320068_0009087208_10_ref.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (115kB) | Request a copy
[thumbnail of RAMA_24201_03031181320068_0009087208_11_lamp.pdf] Text
RAMA_24201_03031181320068_0009087208_11_lamp.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (3MB) | Request a copy

Abstract

Pabrik pembuatan Etilbenzena direncanakan berlokasi di daerah Kawasan Industri Cikarang,Jawa Barat. Pabrik ini meliputi area seluas 8 ( delapan) Ha dengan kapasitas 280.000 ton per tahun. Proses pembuatan Etilbenzena dilakukan dengan Proses oksidatif kopling metana yaitu dengan mereaksikan Metan dalam Fase Gas dengan Oksigen yang berlangsung di dalam Reaktor-01 (R-01) pada temperatur 800°C dan tekanan 22 atm sehingga Menghasilkan bahan baku pembuatan etilbenzena yaitu etilena. Etilena akan direaksikan kembali dengan benzena fasa cair pada reaktor (R-02) pada temperatur 225°C dan tekanan 15 atm sehingga rnenghasilkan etilbenzena,reaksi yang terjadi adalah sebagai berikut : C2H4+ C6H6 C3Hw Pabrik ini merupakan perusahaan yang berbentuk Perseroan Terbatas (PT) dengan sistem organisasi line and staff: yang dipimpin oleh seorang direktur utama dengan jumlah karyav,an 145 orang. Berdasarkan hasil analisa ekonomi, maka Pabrik Etilbenzena ini dinyatakan layak didirikan, diantaranya: a. Total Capital Investment (TCl): US$ 32,898,67i _70 b. Biaya produksi per tahun : US$ 361,459,103.87 c. Total penjualan per tahun : US$ 399,455,788.98 d. Laba bersih per tahun : US$ 27,838,551.55 e. Annual Cash Flow (ACF) : US$ 30,380,721.63 f. Pay Out Time : 2 tahun g. Rate ofreturn on Investment : 85% h. Break Even Point : 36% i. Service life : 11 tahun

Item Type: Thesis (Undergraduate)
Subjects: T Technology > TA Engineering (General). Civil engineering (General) > TA401-492 Materials of engineering and construction. Mechanics of materials > TA418.9.C6.B538 Composite materials. Polymeric composites. Fibrous composites. Biomass chemicals. TECHNOLOGY & ENGINEERING / Material Science. SCIENCE / Chemistry / General
Divisions: 03-Faculty of Engineering > 24201-Chemical Engineering (S1)
Depositing User: IHSANUL RIJAL
Date Deposited: 10 Jan 2022 08:08
Last Modified: 10 Jan 2022 08:08
URI: http://repository.unsri.ac.id/id/eprint/61007

Actions (login required)

View Item View Item