PRA RANCANGAN PABRIK PEMBUATAN DIKLOROPROPANOL KAPASITAS 50.000 TON/TAHUN

GINTING, LEONARDO ROCHA and Sari, Tuti Indah (2019) PRA RANCANGAN PABRIK PEMBUATAN DIKLOROPROPANOL KAPASITAS 50.000 TON/TAHUN. Undergraduate thesis, Sriwijaya University.

[thumbnail of RAMA_24201_03031281419087.pdf] Text
RAMA_24201_03031281419087.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (4MB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_01_Front_Ref.pdf]
Preview
Text
RAMA_24201_03031281419087_0001027501_01_Front_Ref.pdf - Accepted Version
Available under License Creative Commons Public Domain Dedication.

Download (584kB) | Preview
[thumbnail of RAMA_24201_03031281419087_0001027501_02.pdf] Text
RAMA_24201_03031281419087_0001027501_02.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (353kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_03.pdf] Text
RAMA_24201_03031281419087_0001027501_03.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (483kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_04.pdf] Text
RAMA_24201_03031281419087_0001027501_04.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (308kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_05.pdf] Text
RAMA_24201_03031281419087_0001027501_05.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (396kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_06.pdf] Text
RAMA_24201_03031281419087_0001027501_06.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (617kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_07.pdf] Text
RAMA_24201_03031281419087_0001027501_07.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (443kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_08.pdf] Text
RAMA_24201_03031281419087_0001027501_08.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (492kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_09.pdf] Text
RAMA_24201_03031281419087_0001027501_09.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (101kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_10_ref.pdf] Text
RAMA_24201_03031281419087_0001027501_10_ref.pdf - Bibliography
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (193kB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_0001027501_11_lamp.pdf] Text
RAMA_24201_03031281419087_0001027501_11_lamp.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (3MB) | Request a copy
[thumbnail of RAMA_24201_03031281419087_TURNITIN.pdf] Text
RAMA_24201_03031281419087_TURNITIN.pdf - Accepted Version
Restricted to Repository staff only
Available under License Creative Commons Public Domain Dedication.

Download (58MB) | Request a copy

Abstract

The Dichloropropanol plant is planned to be established in 2023, located in the City of Cilegon, Banten Province, Indonesia. This factory covers an area of ​​5 hectares with a capacity of 50,000 tons per year. The process of making Dichloropropanol is done by reacting glycerol and hydrochloric acid with the help of a catalyst of malonic acid which takes place in a stirred tank reactor type reactor at a temperature of 80oC and a pressure of 1.01 bar with the following reaction: C3H8O3 (l) + HCl (l) C3H6Cl2O (l) + 2 H2O (l) This factory is a company in the form of a Limited Liability Company (PT) with a line and staff organization system, which is led by a managing director with 160 employees. Based on the results of an economic analysis, the Dichloropropanol plant was declared feasible to be established with the following economic analysis: • Investment Cost = US $ 358,211,521.67 • Annual sales results = US $ 590,751,563.11 • Annual production costs = US $ 383,116,102.02 • Net profit per year = US $ 134,963,049.70 • Pay Out time = 3.18 years • Rate of return on investment = 37.68% • Discounted Cash Flow –ROR = 36.86% • Break Even Point = 37.73% • Service Life = 11 years Keywords: Stirred tank reactor, chlorination, dichloropropanol

Item Type: Thesis (Undergraduate)
Uncontrolled Keywords: Continious Stirred Tank Reactor, Dichlorpropanol, Chlorination
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 2751 not found.
Date Deposited: 28 Oct 2019 07:43
Last Modified: 28 Oct 2019 07:43
URI: http://repository.unsri.ac.id/id/eprint/13468

Actions (login required)

View Item View Item