#TITLE_ALTERNATIVE#

Indonesia as the second biggest crude palm oil (CPO) producer is predicted to be the biggest producer of CPO by 2010. Thus, this target has triggered the CPO industries. Conventionally, phases necessary to produce CPO can be differed into four major phases (i.e. pre-processing, oil extracting, oil c...

Full description

Saved in:
Bibliographic Details
Main Author: SUSILO (NIM 13003071), ADI
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/9793
Tags: Add Tag
No Tags, Be the first to tag this record!
Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:9793
spelling id-itb.:97932017-09-27T11:39:34Z#TITLE_ALTERNATIVE# SUSILO (NIM 13003071), ADI Indonesia Final Project INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/9793 Indonesia as the second biggest crude palm oil (CPO) producer is predicted to be the biggest producer of CPO by 2010. Thus, this target has triggered the CPO industries. Conventionally, phases necessary to produce CPO can be differed into four major phases (i.e. pre-processing, oil extracting, oil clarification, and mud processing). Problems occurred nowadays is the time spent on oil clarification which is done conventionally. Therefore, a technique called membrane technology has been developed to shorten process. The lesser time needed, the lesser the production cost will be. And better yet, the production will be much faster.<p> <br /> <br /> <br /> This research has two major phases. They are pre-treatment of CPO produced by vibrating screen unit and evaluation on clarification membrane performance. CPO pre-treatment was done by removing large size of insoluble impurities with centrifuged to lighten the work of the membrane. Performance of the membrane in CPO clarification process was evaluated through analysis on the fluxes value, percentage of insoluble impurities, and also water content of CPO that was being produced from each operational condition variation. Cross flow membrane filtration temperatures were varied from 40°C, 50°C, and 60°C; trans membrane pressures (TMP) used 1,5 bar 1,7 bar, and 2,2 bar; and the backflushing intervals for this research used 3, 5, and 7 minutes. The permeate quality which has reach the requirements in conventional clarification unit showed that hydrophobic microporous hollow fiber membrane could be used for clarification process in CPO industries. From the results also proved that operation temperatures, TMP, and backflushing intervals influenced the permeate fluxes. 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 Indonesia as the second biggest crude palm oil (CPO) producer is predicted to be the biggest producer of CPO by 2010. Thus, this target has triggered the CPO industries. Conventionally, phases necessary to produce CPO can be differed into four major phases (i.e. pre-processing, oil extracting, oil clarification, and mud processing). Problems occurred nowadays is the time spent on oil clarification which is done conventionally. Therefore, a technique called membrane technology has been developed to shorten process. The lesser time needed, the lesser the production cost will be. And better yet, the production will be much faster.<p> <br /> <br /> <br /> This research has two major phases. They are pre-treatment of CPO produced by vibrating screen unit and evaluation on clarification membrane performance. CPO pre-treatment was done by removing large size of insoluble impurities with centrifuged to lighten the work of the membrane. Performance of the membrane in CPO clarification process was evaluated through analysis on the fluxes value, percentage of insoluble impurities, and also water content of CPO that was being produced from each operational condition variation. Cross flow membrane filtration temperatures were varied from 40°C, 50°C, and 60°C; trans membrane pressures (TMP) used 1,5 bar 1,7 bar, and 2,2 bar; and the backflushing intervals for this research used 3, 5, and 7 minutes. The permeate quality which has reach the requirements in conventional clarification unit showed that hydrophobic microporous hollow fiber membrane could be used for clarification process in CPO industries. From the results also proved that operation temperatures, TMP, and backflushing intervals influenced the permeate fluxes.
format Final Project
author SUSILO (NIM 13003071), ADI
spellingShingle SUSILO (NIM 13003071), ADI
#TITLE_ALTERNATIVE#
author_facet SUSILO (NIM 13003071), ADI
author_sort SUSILO (NIM 13003071), ADI
title #TITLE_ALTERNATIVE#
title_short #TITLE_ALTERNATIVE#
title_full #TITLE_ALTERNATIVE#
title_fullStr #TITLE_ALTERNATIVE#
title_full_unstemmed #TITLE_ALTERNATIVE#
title_sort #title_alternative#
url https://digilib.itb.ac.id/gdl/view/9793
_version_ 1820664797734109184