PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN

The process of making acrylic acid from glycerol occurs through two steps. The first step is the dehydration reaction of glycerol to acrolein and water. At this step also a side reaction occurs to form acetaldehyde. This reaction takes place in the adiabatic fixed bed reactor using catalysts tungste...

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Main Authors: , DEDE SETIADI, , Ir. Hary Sulistyo, S.U., Ph.D.
Format: Theses and Dissertations NonPeerReviewed
Published: [Yogyakarta] : Universitas Gadjah Mada 2013
Subjects:
ETD
Online Access:https://repository.ugm.ac.id/125395/
http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=65563
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spelling id-ugm-repo.1253952016-03-04T08:29:37Z https://repository.ugm.ac.id/125395/ PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN , DEDE SETIADI , Ir. Hary Sulistyo, S.U., Ph.D. ETD The process of making acrylic acid from glycerol occurs through two steps. The first step is the dehydration reaction of glycerol to acrolein and water. At this step also a side reaction occurs to form acetaldehyde. This reaction takes place in the adiabatic fixed bed reactor using catalysts tungsten-Zircon in the gas phase at 310 0C temperature and pressure of 2 atm. Then on the next step acrolein is oxidized by oxygen in a fixed bed reactor multitube with catalyst Mo12V4Cu2Fe. Because of the highly exothermic reaction, dowtherm A is used to keep the temperature between 310 and 350 °C. The need for water utilities include as much as 642,194.5248 tons / year obtained from the Cisadane river. Steam as much as 127,661.7024 tons / year generated by the boiler, fuel oil as much as 185.328 tons / year and dowterm A as much as 388.8 tons / years. Acrylic acid plant with a capacity of 20,000 tons per year will be established in Tangerang, Banten with a land area of 2 hectares and employees 150 people. The plant uses glycerol as the main raw material 38,793.6 tons / year. Fixed capital investment of Rp 74.144.776,381 + $ 9,991,569.43 working capital of Rp 11.831.225,406 + $ 10,325,803.68. ROI before taxes 36.90%, and 18.45% ROI after tax before tax while POT is 2.13 years and 3.52 years after tax. Break-even point 47.18%, shut down point 30.01% and DCFRR 38.09%. In terms of the economy and the need for the establishment of acrylic acid plant in Indonesia, the plant with a capacity of 20,000 tonnes per year is quite exciting to be re-examined to set up in Indonesia [Yogyakarta] : Universitas Gadjah Mada 2013 Thesis NonPeerReviewed , DEDE SETIADI and , Ir. Hary Sulistyo, S.U., Ph.D. (2013) PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN. UNSPECIFIED thesis, UNSPECIFIED. http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=65563
institution Universitas Gadjah Mada
building UGM Library
country Indonesia
collection Repository Civitas UGM
topic ETD
spellingShingle ETD
, DEDE SETIADI
, Ir. Hary Sulistyo, S.U., Ph.D.
PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN
description The process of making acrylic acid from glycerol occurs through two steps. The first step is the dehydration reaction of glycerol to acrolein and water. At this step also a side reaction occurs to form acetaldehyde. This reaction takes place in the adiabatic fixed bed reactor using catalysts tungsten-Zircon in the gas phase at 310 0C temperature and pressure of 2 atm. Then on the next step acrolein is oxidized by oxygen in a fixed bed reactor multitube with catalyst Mo12V4Cu2Fe. Because of the highly exothermic reaction, dowtherm A is used to keep the temperature between 310 and 350 °C. The need for water utilities include as much as 642,194.5248 tons / year obtained from the Cisadane river. Steam as much as 127,661.7024 tons / year generated by the boiler, fuel oil as much as 185.328 tons / year and dowterm A as much as 388.8 tons / years. Acrylic acid plant with a capacity of 20,000 tons per year will be established in Tangerang, Banten with a land area of 2 hectares and employees 150 people. The plant uses glycerol as the main raw material 38,793.6 tons / year. Fixed capital investment of Rp 74.144.776,381 + $ 9,991,569.43 working capital of Rp 11.831.225,406 + $ 10,325,803.68. ROI before taxes 36.90%, and 18.45% ROI after tax before tax while POT is 2.13 years and 3.52 years after tax. Break-even point 47.18%, shut down point 30.01% and DCFRR 38.09%. In terms of the economy and the need for the establishment of acrylic acid plant in Indonesia, the plant with a capacity of 20,000 tonnes per year is quite exciting to be re-examined to set up in Indonesia
format Theses and Dissertations
NonPeerReviewed
author , DEDE SETIADI
, Ir. Hary Sulistyo, S.U., Ph.D.
author_facet , DEDE SETIADI
, Ir. Hary Sulistyo, S.U., Ph.D.
author_sort , DEDE SETIADI
title PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN
title_short PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN
title_full PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN
title_fullStr PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN
title_full_unstemmed PRARANCANGAN PABRIK ASAM AKRILAT DARI GLISEROL KAPASITAS 20.000 TON PER TAHUN
title_sort prarancangan pabrik asam akrilat dari gliserol kapasitas 20.000 ton per tahun
publisher [Yogyakarta] : Universitas Gadjah Mada
publishDate 2013
url https://repository.ugm.ac.id/125395/
http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=65563
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