PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN

Preliminary design of Terephtalic Acid Plant from Paraxylene and Air with production capacity of 300,000 ton/year is intended to fulfill terephtalic acid demands, hopefully also fulfill demands from foreign country. In order to fulfill the demands, 192.626,28 ton/year of paraxylene , 19.761,98 ton/y...

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Main Authors: , MUHAMMAD SILVANO IBRAHIM AIWAN, , Prof. Ir. Suryo Purwono, MA., Sc., Ph.D.
Format: Theses and Dissertations NonPeerReviewed
Published: [Yogyakarta] : Universitas Gadjah Mada 2014
Subjects:
ETD
Online Access:https://repository.ugm.ac.id/132500/
http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=73035
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spelling id-ugm-repo.1325002016-03-04T08:01:15Z https://repository.ugm.ac.id/132500/ PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN , MUHAMMAD SILVANO IBRAHIM AIWAN , Prof. Ir. Suryo Purwono, MA., Sc., Ph.D. ETD Preliminary design of Terephtalic Acid Plant from Paraxylene and Air with production capacity of 300,000 ton/year is intended to fulfill terephtalic acid demands, hopefully also fulfill demands from foreign country. In order to fulfill the demands, 192.626,28 ton/year of paraxylene , 19.761,98 ton/year of acetic acid, and 1926,27 ton/year of cobalt (II) acetic are needed. . The main components react in 3 parallel CSTR reactors which operated isothermally in 2000C and the pressure is 20 atm. Because of very exothermic reaction to maintain the temperature in the reactor, there is coil cooling system. Utility needed to extend the process system consist of.4.854.581 ton/year demineralized water, 3446kW/year of electricity, 6.826.127,04 US gal/year of industrial fuel, dan 272.544,07 ton/year of saturated steam. The plant will be established in Kawasan Industri Cilacap (KCI) because the location near to PERTAMINA RU IV Cilacap that provide paraxylenes. Beside of that, the location of the plant also near to market targets which are Dimethyl Terephtalat and Pure Terephtalic Acid company that spreaded especially in Java. The area of the plant is 180.000m2 and 228 of manpower are needed. Fixed capital needed is Rp 353,169,858,507,00 + $ 57,551,956 and working capital of Rp 35.079.489.855,00 + $ 95.780.247,00. Based on economic analysis, the Return On Investment before tax is 59,74% and after tax is 28,79%. Pay Out Time befora tax is 1,31 year and after tax is 2,58 year. Break Even Point is 45,52 %, Shut Down Point is 30,03 % and Discounted Cash Flow Rate Of Return is 30,70 %. Therefore, further research on Terephtalic Acid Plant from Paraxylene and Air with production capacity of 300.000 ton/year should be carried out. [Yogyakarta] : Universitas Gadjah Mada 2014 Thesis NonPeerReviewed , MUHAMMAD SILVANO IBRAHIM AIWAN and , Prof. Ir. Suryo Purwono, MA., Sc., Ph.D. (2014) PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN. UNSPECIFIED thesis, UNSPECIFIED. http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=73035
institution Universitas Gadjah Mada
building UGM Library
country Indonesia
collection Repository Civitas UGM
topic ETD
spellingShingle ETD
, MUHAMMAD SILVANO IBRAHIM AIWAN
, Prof. Ir. Suryo Purwono, MA., Sc., Ph.D.
PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN
description Preliminary design of Terephtalic Acid Plant from Paraxylene and Air with production capacity of 300,000 ton/year is intended to fulfill terephtalic acid demands, hopefully also fulfill demands from foreign country. In order to fulfill the demands, 192.626,28 ton/year of paraxylene , 19.761,98 ton/year of acetic acid, and 1926,27 ton/year of cobalt (II) acetic are needed. . The main components react in 3 parallel CSTR reactors which operated isothermally in 2000C and the pressure is 20 atm. Because of very exothermic reaction to maintain the temperature in the reactor, there is coil cooling system. Utility needed to extend the process system consist of.4.854.581 ton/year demineralized water, 3446kW/year of electricity, 6.826.127,04 US gal/year of industrial fuel, dan 272.544,07 ton/year of saturated steam. The plant will be established in Kawasan Industri Cilacap (KCI) because the location near to PERTAMINA RU IV Cilacap that provide paraxylenes. Beside of that, the location of the plant also near to market targets which are Dimethyl Terephtalat and Pure Terephtalic Acid company that spreaded especially in Java. The area of the plant is 180.000m2 and 228 of manpower are needed. Fixed capital needed is Rp 353,169,858,507,00 + $ 57,551,956 and working capital of Rp 35.079.489.855,00 + $ 95.780.247,00. Based on economic analysis, the Return On Investment before tax is 59,74% and after tax is 28,79%. Pay Out Time befora tax is 1,31 year and after tax is 2,58 year. Break Even Point is 45,52 %, Shut Down Point is 30,03 % and Discounted Cash Flow Rate Of Return is 30,70 %. Therefore, further research on Terephtalic Acid Plant from Paraxylene and Air with production capacity of 300.000 ton/year should be carried out.
format Theses and Dissertations
NonPeerReviewed
author , MUHAMMAD SILVANO IBRAHIM AIWAN
, Prof. Ir. Suryo Purwono, MA., Sc., Ph.D.
author_facet , MUHAMMAD SILVANO IBRAHIM AIWAN
, Prof. Ir. Suryo Purwono, MA., Sc., Ph.D.
author_sort , MUHAMMAD SILVANO IBRAHIM AIWAN
title PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN
title_short PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN
title_full PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN
title_fullStr PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN
title_full_unstemmed PRARANCANGAN PABRIK ASAM TEREFTALAT DARI PARAXYLENE DAN UDARA KAPASITAS 300.000 TON/TAHUN
title_sort prarancangan pabrik asam tereftalat dari paraxylene dan udara kapasitas 300.000 ton/tahun
publisher [Yogyakarta] : Universitas Gadjah Mada
publishDate 2014
url https://repository.ugm.ac.id/132500/
http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=73035
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