PRA RANCANGAN PABRIK PEMBUATAN NEOPENTANE KAPASITAS 115.000 TON/TAHUN

WIRAWAN, HABIL MAJID and SAKINAH, FRISKHA HANIFAH and Nasir, Subriyer (2019) PRA RANCANGAN PABRIK PEMBUATAN NEOPENTANE KAPASITAS 115.000 TON/TAHUN. Undergraduate thesis, Sriwijaya University.

	Text RAMA_24201_03031181520002_03031181520017.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (25MB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_TURNITIN.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (23MB) | Request a copy
Preview	Text RAMA_24201_03031181520002_03031181520017_009096003_01_front_ref.pdf - Accepted Version Available under License Creative Commons Public Domain Dedication. Download (1MB) | Preview
	Text RAMA_24201_03031181520002_03031181520017_009096003_02.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (279kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_03.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (336kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_03.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (336kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_04.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (132kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_05.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (132kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_06.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (171kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_07.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (222kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_08.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (585kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_09.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (101kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_10_ref.pdf - Bibliography Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (70kB) | Request a copy
	Text RAMA_24201_03031181520002_03031181520017_009096003_11_lamp.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (4MB) | Request a copy

Abstract

Pabrik Neopentane direncanakan berlokasi di daerah Cilegon, Banten. Pabrik ini meliputi area seluas 7 Ha dengan kapasitas 115.000 ton pertahun. Proses pembuatan Neopentane dilakukan dalam dua tahap proses, yaitu reaksi Dimerisasi Isobutilen menjadi Diisobutilen dengan bantuan katalis Amberlyst-15 yang berlangsung di Reaktor Tubular Fixed Bed (R-01) pada temperatur 56oC dan tekanan 7,85 bar. Sedangkan reaksi kedua yaitu reaksi Demetilasi Diisobutilen dengan hidrogen menggunakan bantuan katalis Ni on Kieselguhr yang berlangsung di Reaktor Tubular Fixed Bed (R-02) pada temperatur 285oC dan tekanan 3,1 bar dengan reaksi sebagai berikut : Reaksi pada Reaktor-01 Dimerisasi Isobutilen: 2C4H8 -> C8H16 (Isobutilena) -> (Diisobutilena) Reaksi pada Reaktor-02 Hidrogenasi Diisobutilena: C8H16 + 4H2 -> C5H12 + 3CH4 (2,4,4-trimetil pentena) + (Hidrogen) -> (2,2-dimetil propana) + (Metana) Pabrik ini merupakan perusahaan yang berbentuk Perseroan Terbatas (PT) dengan sistem organisasi line and staff, yang dipimpin oleh seorang General Manager dengan jumlah karyawan 136 orang. Berdasarkan hasil analisa ekonomi, Pabrik Neopentane dinyatakan layak untuk didirikan dengan analisa ekonomi sebagai berikut: Total Capital Investment = US $ 111.631.793,57 Selling Price per Year = US $ 285.802.902,63 Total Production Cost = US $ 209.295.121,34 Annual Cash Flow = US $ 64.761.524,23 Pay Out Time = 1,84 tahun Rate of return on investment = 51,40 % Discounted Cash Flow –ROR = 56,54 % Break Even Point = 33,37 % Service Life = 11 tahun

Item Type:	Thesis (Undergraduate)
Uncontrolled Keywords:	Pra Rancangan Pabrik, Neopentane, Chemical Engineering Project Plant
Subjects:	T Technology > TP Chemical technology > TP155-156 Chemical engineering > TP155.5P4 Chemical plants--Design and construction
Divisions:	03-Faculty of Engineering > 24201-Chemical Engineering (S1)
Depositing User:	Users 2470 not found.
Date Deposited:	16 Oct 2019 07:50
Last Modified:	16 Oct 2019 07:50
URI:	http://repository.unsri.ac.id/id/eprint/11784

Actions (login required)

View Item