PRA RENCANA PABRIK PEMBUATAN HIDROGEN FLUORIDA KAPASITAS PRODUKSI 10.000 TON/TAHUN

RIFKI, MUHAMMAD RIZWAN and THOHIROZARA, DHIMAS FAUZAN and Komariah, Leily Nurul (2019) PRA RENCANA PABRIK PEMBUATAN HIDROGEN FLUORIDA KAPASITAS PRODUKSI 10.000 TON/TAHUN. Undergraduate thesis, Sriwijaya University.

	Text RAMA_24201_03031181419046_03031381419117.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (16MB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_TURNITIN.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (31MB) | Request a copy
Preview	Text RAMA_24201_03031181419046_03031381419117_0026037502_01_front ref.pdf - Accepted Version Available under License Creative Commons Public Domain Dedication. Download (623kB) | Preview
	Text RAMA_24201_03031181419046_03031381419117_0026037502_02.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (208kB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_0026037502_03.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (267kB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_0026037502_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_03031181419046_03031381419117_0026037502_05.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (376kB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_0026037502_06.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (262kB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_0026037502_07.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (431kB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_0026037502_08.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (341kB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_0026037502_09.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (8kB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_0026037502_06_ref.pdf - Bibliography Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (148kB) | Request a copy
	Text RAMA_24201_03031181419046_03031381419117_0026037502_07_lamp.pdf - Accepted Version Restricted to Repository staff only Available under License Creative Commons Public Domain Dedication. Download (2MB) | Request a copy

Abstract

This Hydrogen Fluoride plant is planned to be built in Gresik, East Java. Covers an area of 5 hectares with a capacity of 10.000 tons/year. The proecss of making Hydrogen Fluoride uses fluorspar and sulfuric acid as raw materials. The reaction takes place at a pressure of 1 atm and a temperature of 105°C (US 9,656,864 B2). The reactor used is a Kiln. The reaction is as follows : Reaction 1 : CaF2 + H2O  CaSO4 + 2HF Reaction 2 : CaCO3 + H2SO4  CaSO4 + CO2 + H2O Reaction 3 : SiO2 + 4HF  SiF4 + 2H2O This company is planned to take the form of a Limited Liability Company (Perseroan Terbatas/PT) with a line and staff organization system, led by a managing director with 112 employees. Based on the results of economic analysis calculation, this Hydrogen Fluoride manufaturing plant is feasible enough to be built. Based on the following economic analysis:  Total Capital Investment = US $ 24.068.558,27  Sales Results per year = US $ 31.164.681,60  Production Cost per year = US $ 17.312.898,47  Annual Cash Flow = US $ 11.540.659,81  Pay Out time = 3,13 tahun  Rate of return on investment = 38,27 %  Discounted Cash Flow –ROR = 57,43 %  Break Even Point = 25,87 %  Service Life = 11 tahun

Item Type:	Thesis (Undergraduate)
Uncontrolled Keywords:	Teknik kimia, Rancangan Pabrik
Subjects:	T Technology > TP Chemical technology > TP155-156 Chemical engineering
Divisions:	03-Faculty of Engineering > 24201-Chemical Engineering (S1)
Depositing User:	Users 2069 not found.
Date Deposited:	25 Sep 2019 06:32
Last Modified:	25 Sep 2019 06:32
URI:	http://repository.unsri.ac.id/id/eprint/8813

Actions (login required)

View Item