PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN

Production facility of chloroform is designed with a capacity of 25.000 tons/year and operated continuously for 330 days/year and 24 hours/day. The product obtained is chloroform with purity 99,60%. The raw materials used are sodium hydroxide 48% as much as 14.838,18 kg/hr, acetone as much as1.549,2...

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Main Authors: , RAHMITA PUSPA NINTIA, , Ir. Moh. Fahrurrozi, M.Sc., Ph.D.
Format: Theses and Dissertations NonPeerReviewed
Published: [Yogyakarta] : Universitas Gadjah Mada 2013
Subjects:
ETD
Online Access:https://repository.ugm.ac.id/124094/
http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=64213
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spelling id-ugm-repo.1240942016-03-04T08:42:08Z https://repository.ugm.ac.id/124094/ PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN , RAHMITA PUSPA NINTIA , Ir. Moh. Fahrurrozi, M.Sc., Ph.D. ETD Production facility of chloroform is designed with a capacity of 25.000 tons/year and operated continuously for 330 days/year and 24 hours/day. The product obtained is chloroform with purity 99,60%. The raw materials used are sodium hydroxide 48% as much as 14.838,18 kg/hr, acetone as much as1.549,26 kg/hr and chlorine as much as 6.386,20 kg/hr. Processes used inthe manufacture ofchloroformis ketones reduction,in this case is acetone. The process starts with the synthesis of sodium hypochlorite from sodium hydroxide and chlorine. Sodium hypochlorite solution reacts with acetone in a continuous stirred tank reactor. This reaction occurs in the liquid phase and takes place at a temperature of 60-75oC and 2 atm pressure. The heat of reaction is absorbed by the cooling water flowing in cooling coil and cooling jacket. The plant will be built at Cilegon, Province of Banten with a land area of 30 ha and will employ 188 personels. The plant needs 46.144,09 ton/year of steams, 77.995,85ton/year of water, 170.457,41 ton/year of natural gas, and 23.760.000 kWh/year of electricity. Fixed capital investment required is US$ 19.790.347,47 + Rp 186.934.848.123,18 [Yogyakarta] : Universitas Gadjah Mada 2013 Thesis NonPeerReviewed , RAHMITA PUSPA NINTIA and , Ir. Moh. Fahrurrozi, M.Sc., Ph.D. (2013) PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN. UNSPECIFIED thesis, UNSPECIFIED. http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=64213
institution Universitas Gadjah Mada
building UGM Library
country Indonesia
collection Repository Civitas UGM
topic ETD
spellingShingle ETD
, RAHMITA PUSPA NINTIA
, Ir. Moh. Fahrurrozi, M.Sc., Ph.D.
PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN
description Production facility of chloroform is designed with a capacity of 25.000 tons/year and operated continuously for 330 days/year and 24 hours/day. The product obtained is chloroform with purity 99,60%. The raw materials used are sodium hydroxide 48% as much as 14.838,18 kg/hr, acetone as much as1.549,26 kg/hr and chlorine as much as 6.386,20 kg/hr. Processes used inthe manufacture ofchloroformis ketones reduction,in this case is acetone. The process starts with the synthesis of sodium hypochlorite from sodium hydroxide and chlorine. Sodium hypochlorite solution reacts with acetone in a continuous stirred tank reactor. This reaction occurs in the liquid phase and takes place at a temperature of 60-75oC and 2 atm pressure. The heat of reaction is absorbed by the cooling water flowing in cooling coil and cooling jacket. The plant will be built at Cilegon, Province of Banten with a land area of 30 ha and will employ 188 personels. The plant needs 46.144,09 ton/year of steams, 77.995,85ton/year of water, 170.457,41 ton/year of natural gas, and 23.760.000 kWh/year of electricity. Fixed capital investment required is US$ 19.790.347,47 + Rp 186.934.848.123,18
format Theses and Dissertations
NonPeerReviewed
author , RAHMITA PUSPA NINTIA
, Ir. Moh. Fahrurrozi, M.Sc., Ph.D.
author_facet , RAHMITA PUSPA NINTIA
, Ir. Moh. Fahrurrozi, M.Sc., Ph.D.
author_sort , RAHMITA PUSPA NINTIA
title PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN
title_short PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN
title_full PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN
title_fullStr PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN
title_full_unstemmed PABRIK KLOROFORM DARI NATRIUM HIDROKSIDA, KLORIN, DAN ASETON KAPASITAS 25.000 TON/TAHUN
title_sort pabrik kloroform dari natrium hidroksida, klorin, dan aseton kapasitas 25.000 ton/tahun
publisher [Yogyakarta] : Universitas Gadjah Mada
publishDate 2013
url https://repository.ugm.ac.id/124094/
http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=64213
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