CONTINUOUS SYNGAS FERMENTATION BY CLOSTRIDIUM LJUNGDAHLII IN A CONTINUOUS STIRRED TANK REACTOR WITH HOLLOW FIBER MEMBRANE

Biomass is a renewable resource with high potential as raw material for energy source. One example of biomass utilization is via gasification to produce synthetic gas (syngas) which can be converted to ethanol. Current emerging process is fermenting the syngas which can be done in modest temperature...

Full description

Saved in:
Bibliographic Details
Main Author: Adisurya Ismail, Guntur
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/42307
Tags: Add Tag
No Tags, Be the first to tag this record!
Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:42307
spelling id-itb.:423072019-09-18T11:07:42ZCONTINUOUS SYNGAS FERMENTATION BY CLOSTRIDIUM LJUNGDAHLII IN A CONTINUOUS STIRRED TANK REACTOR WITH HOLLOW FIBER MEMBRANE Adisurya Ismail, Guntur Indonesia Theses Fermentation, syngas, bioethanol, dilution rate, hollow fiber membrane INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/42307 Biomass is a renewable resource with high potential as raw material for energy source. One example of biomass utilization is via gasification to produce synthetic gas (syngas) which can be converted to ethanol. Current emerging process is fermenting the syngas which can be done in modest temperature and pressure. There are many factors that can affect the fermentation, and one of them is the operation mode. This thesis presents the result of continuous syngas fermentation by Clostridium ljungdahlii compared to batch fermentation, based on the concentration of the cell, acetate, and ethanol, as well as the syngas utilization rate. Fermentation process is done in two steps. First step is batch fermentation which is done in 10-14 days. The next step is the continuous fermentation. Dilution rate of 0,015 hour-1 and 0,007 hour-1 is used to determine the effect of dilution rate towards the result of the fermentation. Hollow fiber membrane will be used from the second day for media recirculation to improve the gas-liquid transfer rate. Cell concentration is measured using spectrophotometer, ethanol and acetate is measured via HPLC while gas composition in the headspace is determined by using GC. Continuous fermentation with dilution rate of 0,015 hour-1 will produce 2,12 g/L of acetate, 0,09 g/L of ethanol, and 0,56 g/L of biomass. On the other hand, fermentation with dilution rate of 0,007 hour-1 produce 1,05 g/L of acetate, 0,58 g/L of ethanol, and 0,37 g/L of biomass. Increasing the dilution rate will promote the cell growth, but gives opposite effect towards ethanol production which is non-growth associated product. The improvement of cell activities is also proven with the increase in the CO consumption rate which is higher for bigger dilution rate (36% for dilution rate of 0,015 hour-1, compared to 27% for dilution rate of 0,007 hour-1) 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 Biomass is a renewable resource with high potential as raw material for energy source. One example of biomass utilization is via gasification to produce synthetic gas (syngas) which can be converted to ethanol. Current emerging process is fermenting the syngas which can be done in modest temperature and pressure. There are many factors that can affect the fermentation, and one of them is the operation mode. This thesis presents the result of continuous syngas fermentation by Clostridium ljungdahlii compared to batch fermentation, based on the concentration of the cell, acetate, and ethanol, as well as the syngas utilization rate. Fermentation process is done in two steps. First step is batch fermentation which is done in 10-14 days. The next step is the continuous fermentation. Dilution rate of 0,015 hour-1 and 0,007 hour-1 is used to determine the effect of dilution rate towards the result of the fermentation. Hollow fiber membrane will be used from the second day for media recirculation to improve the gas-liquid transfer rate. Cell concentration is measured using spectrophotometer, ethanol and acetate is measured via HPLC while gas composition in the headspace is determined by using GC. Continuous fermentation with dilution rate of 0,015 hour-1 will produce 2,12 g/L of acetate, 0,09 g/L of ethanol, and 0,56 g/L of biomass. On the other hand, fermentation with dilution rate of 0,007 hour-1 produce 1,05 g/L of acetate, 0,58 g/L of ethanol, and 0,37 g/L of biomass. Increasing the dilution rate will promote the cell growth, but gives opposite effect towards ethanol production which is non-growth associated product. The improvement of cell activities is also proven with the increase in the CO consumption rate which is higher for bigger dilution rate (36% for dilution rate of 0,015 hour-1, compared to 27% for dilution rate of 0,007 hour-1)
format Theses
author Adisurya Ismail, Guntur
spellingShingle Adisurya Ismail, Guntur
CONTINUOUS SYNGAS FERMENTATION BY CLOSTRIDIUM LJUNGDAHLII IN A CONTINUOUS STIRRED TANK REACTOR WITH HOLLOW FIBER MEMBRANE
author_facet Adisurya Ismail, Guntur
author_sort Adisurya Ismail, Guntur
title CONTINUOUS SYNGAS FERMENTATION BY CLOSTRIDIUM LJUNGDAHLII IN A CONTINUOUS STIRRED TANK REACTOR WITH HOLLOW FIBER MEMBRANE
title_short CONTINUOUS SYNGAS FERMENTATION BY CLOSTRIDIUM LJUNGDAHLII IN A CONTINUOUS STIRRED TANK REACTOR WITH HOLLOW FIBER MEMBRANE
title_full CONTINUOUS SYNGAS FERMENTATION BY CLOSTRIDIUM LJUNGDAHLII IN A CONTINUOUS STIRRED TANK REACTOR WITH HOLLOW FIBER MEMBRANE
title_fullStr CONTINUOUS SYNGAS FERMENTATION BY CLOSTRIDIUM LJUNGDAHLII IN A CONTINUOUS STIRRED TANK REACTOR WITH HOLLOW FIBER MEMBRANE
title_full_unstemmed CONTINUOUS SYNGAS FERMENTATION BY CLOSTRIDIUM LJUNGDAHLII IN A CONTINUOUS STIRRED TANK REACTOR WITH HOLLOW FIBER MEMBRANE
title_sort continuous syngas fermentation by clostridium ljungdahlii in a continuous stirred tank reactor with hollow fiber membrane
url https://digilib.itb.ac.id/gdl/view/42307
_version_ 1822270059152670720