PENGEMBANGAN PROSES PEMBUATAN SELULOSA ASETAT DARI PULP TANDAN KOSONG SAWIT PROSES ETANOL

Being abundant lignocellulosic waste, oil palm empty fruit bunches (EFB) has a great potency as a source of cellulose or pulp. Using ethanosolv-pulping, this agricultural waste could be processed into pulp with an a-cellulose content in the range of 85 - 88%. This research dealt with the conversion...

Full description

Saved in:
Bibliographic Details
Main Author: Maria Amin , Asnetty
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/7346
Tags: Add Tag
No Tags, Be the first to tag this record!
Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:7346
spelling id-itb.:73462017-09-27T14:51:59ZPENGEMBANGAN PROSES PEMBUATAN SELULOSA ASETAT DARI PULP TANDAN KOSONG SAWIT PROSES ETANOL Maria Amin , Asnetty Indonesia Theses INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/7346 Being abundant lignocellulosic waste, oil palm empty fruit bunches (EFB) has a great potency as a source of cellulose or pulp. Using ethanosolv-pulping, this agricultural waste could be processed into pulp with an a-cellulose content in the range of 85 - 88%. This research dealt with the conversion of EFB ethanosolv-pulp into a more valuable cellulose acetate. Two conventional cellulose acetate production processes have been studied experimentally. The conventional Emil Heuser and Celanese processes used in this experimental study have quite different process steps and chemicals. In Emil Heuser process, cellulose is firstly depolimerized into a degree of polimerization of about 130. Acetylation is then carried out slowly to a desired degree of acetylation. H3PO4 and acetic acid glasial are the main chemicals in Emil Heuser process. Acetic anhydride is used to complete acetylation in Celanese process. This acetylation process is then followed by hydrolysis to obtain the desired degree of acetylation. No depolimerization of cellulose is applied in this process. To achieve a spesification of dissolving pulp with a-cellulose contents in the range of 95 - 100%, EFB ethanosolv-pulp must be treated in the following process : a. extended delignification using the CEHEH bleaching process b. further dissolution of 13 and y-cellulose c. extensive washing to remove all impurities Pulps resulted from the above pre-treatments were found to have a sufficiently high a-cellulose content in the range of 90 - 98%. As expected, pretreated EFB ethanosolv pulp could be converted into cellulose acetate having acetyl content in the range 39 - 41% by weight. As cellulose underwent depolimerization in Emil Heuser process, some of cellulose might be lost. Therefore more cellulose as raw material was required in Emil Heuser process than in Celanese process. Emil Heuser process seemed more attractive, since most chemical might be recovered and reused for subsequent process. While dilute acetic acid was the main by products in Celanese. text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description Being abundant lignocellulosic waste, oil palm empty fruit bunches (EFB) has a great potency as a source of cellulose or pulp. Using ethanosolv-pulping, this agricultural waste could be processed into pulp with an a-cellulose content in the range of 85 - 88%. This research dealt with the conversion of EFB ethanosolv-pulp into a more valuable cellulose acetate. Two conventional cellulose acetate production processes have been studied experimentally. The conventional Emil Heuser and Celanese processes used in this experimental study have quite different process steps and chemicals. In Emil Heuser process, cellulose is firstly depolimerized into a degree of polimerization of about 130. Acetylation is then carried out slowly to a desired degree of acetylation. H3PO4 and acetic acid glasial are the main chemicals in Emil Heuser process. Acetic anhydride is used to complete acetylation in Celanese process. This acetylation process is then followed by hydrolysis to obtain the desired degree of acetylation. No depolimerization of cellulose is applied in this process. To achieve a spesification of dissolving pulp with a-cellulose contents in the range of 95 - 100%, EFB ethanosolv-pulp must be treated in the following process : a. extended delignification using the CEHEH bleaching process b. further dissolution of 13 and y-cellulose c. extensive washing to remove all impurities Pulps resulted from the above pre-treatments were found to have a sufficiently high a-cellulose content in the range of 90 - 98%. As expected, pretreated EFB ethanosolv pulp could be converted into cellulose acetate having acetyl content in the range 39 - 41% by weight. As cellulose underwent depolimerization in Emil Heuser process, some of cellulose might be lost. Therefore more cellulose as raw material was required in Emil Heuser process than in Celanese process. Emil Heuser process seemed more attractive, since most chemical might be recovered and reused for subsequent process. While dilute acetic acid was the main by products in Celanese.
format Theses
author Maria Amin , Asnetty
spellingShingle Maria Amin , Asnetty
PENGEMBANGAN PROSES PEMBUATAN SELULOSA ASETAT DARI PULP TANDAN KOSONG SAWIT PROSES ETANOL
author_facet Maria Amin , Asnetty
author_sort Maria Amin , Asnetty
title PENGEMBANGAN PROSES PEMBUATAN SELULOSA ASETAT DARI PULP TANDAN KOSONG SAWIT PROSES ETANOL
title_short PENGEMBANGAN PROSES PEMBUATAN SELULOSA ASETAT DARI PULP TANDAN KOSONG SAWIT PROSES ETANOL
title_full PENGEMBANGAN PROSES PEMBUATAN SELULOSA ASETAT DARI PULP TANDAN KOSONG SAWIT PROSES ETANOL
title_fullStr PENGEMBANGAN PROSES PEMBUATAN SELULOSA ASETAT DARI PULP TANDAN KOSONG SAWIT PROSES ETANOL
title_full_unstemmed PENGEMBANGAN PROSES PEMBUATAN SELULOSA ASETAT DARI PULP TANDAN KOSONG SAWIT PROSES ETANOL
title_sort pengembangan proses pembuatan selulosa asetat dari pulp tandan kosong sawit proses etanol
url https://digilib.itb.ac.id/gdl/view/7346
_version_ 1820664128942899200