PRA RANCANGAN PABRIK PEMBUATAN DIKLOROPROPANOL KAPASITAS 50.000 TON/TAHUN
Total View This Week0
Total View This Week0
Institusion
Universitas Sriwijaya
Author
LEONARDO ROCHA GINTING (STUDENT ID : 03031281419087)
Tuti Indah Sari (LECTURER ID : 0001027501)
Tuti Indah Sari (LECTURER ID : 0001027501)
Subject
TP155.5P4 Chemical plants--Design and construction
Datestamp
2019-10-28 07:43:00
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
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
File :
RAMA_24201_03031281419087.pdf
RAMA_24201_03031281419087_0001027501_01_Front_Ref.pdf
RAMA_24201_03031281419087_0001027501_10_ref.pdf
RAMA_24201_03031281419087_0001027501_11_lamp.pdf
RAMA_24201_03031281419087_TURNITIN.pdf
RAMA_24201_03031281419087_0001027501_02.pdf
RAMA_24201_03031281419087_0001027501_03.pdf
RAMA_24201_03031281419087_0001027501_04.pdf
RAMA_24201_03031281419087_0001027501_05.pdf
RAMA_24201_03031281419087_0001027501_06.pdf
RAMA_24201_03031281419087_0001027501_07.pdf
RAMA_24201_03031281419087_0001027501_08.pdf
RAMA_24201_03031281419087_0001027501_09.pdf
Download
book
BibTex
Latex, Jabref
cloud_download
Original Resource
url resource Institution
