Biohydrogen production from palm oil mill effluent using polyethylene glycol immobilized cells in upflow anaerobic sludge blanket reactor
The demand for improvement of the hydrogen production by dark hydrogen fermentation is increasing. Recently, a number of cell-immobilization systems were used to improve dark hydrogen production. The main objective of this research was to examine the polyethylene glycol immobilized cells system...
| Main Author: | |
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| Format: | Thesis |
| Language: | English |
| Published: |
2013
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| Subjects: | |
| Online Access: | http://umpir.ump.edu.my/id/eprint/9446/ http://umpir.ump.edu.my/id/eprint/9446/ http://umpir.ump.edu.my/id/eprint/9446/1/CD7810.pdf |
| Summary: | The demand for improvement of the hydrogen production by dark hydrogen fermentation is
increasing. Recently, a number of cell-immobilization systems were used to improve dark
hydrogen production. The main objective of this research was to examine the polyethylene
glycol immobilized cells system in enhancing hydrogen production and treatment of palm oil
mill effluent (POME). During this research five experiments were performed. In the first
experiment, PEG gel was fabricated and used as a carrier to immobilize Clostridium sp. for
biohydrogen production using POME. POME was diluted and used as a substrate. The
resulting PEG-immobilized cells were found to yield 5.35 L H
/L-POME, and the maximum
hydrogen production rate was 0.5 L H
2
2
/L-POME/h (22.7 mmol/L h). The Monod-type
kinetic model was used to describe the effect of substrate (POME) concentration on the
hydrogen production rate. Furthermore, PEG- immobilized cell was examined for H
production in comparison to suspended cell reactor. The suspended-cell containing reactor
was able to produce hydrogen at an optimal rate of 0.348 L H
/L-POME/h at HRT 6 h.
However, the immobilized-cell containing reactor exhibited better hydrogen production rate
of 0.589 LH
2
2
/ L-POME/h which occurred at HRT 2 h. When the immobilized-cell
containing reactor was scaled up to 5 L, the hydrogen production rate was 0.553–0.589 L H
/
L-POME/h. Another study addressed the application of a PEG-immobilized upflow
anaerobic sludge blanket (UASB) reactor using Clostridium sp. for enhancing continuous
hydrogen production from POME. The UASB reactor containing immobilized cells was
operated at varying hydraulic retention times (HRT) that ranged from 24 to 6 h at 3.3 g
chemical oxygen demand (COD)/L/h organic loading rate (OLR), or at OLRs that ranged
from 1.6 to 6.6 at 12 h HRT. The maximum volumetric hydrogen production rate of 0.336
LH
2
/L/h (15.0 mmol/L/h) with a hydrogen yield of 0.35 LH
2
/g COD
was obtained at a
HRT of 12 h and an OLR of 5.0 g COD/L/h. The effect of immobilized cell packing ratio,
HRT and POME concentration on continuous hydrogen production and treatment efficiency
of palm oil mill effluent was studied. The UASB reactor with a PEG-immobilized cell
packing ratio of 10% weight to volume ratio (w/v) was optimal for dark hydrogen
production. The highest volumetric hydrogen production rate of 0.365 L H
removed
/L/h (16.2
mmol/L/h) with a hydrogen yield of 0.38 LH
2
/g COD
was obtained at POME
concentration of 30 g COD/L and HRT of 16 h. The average hydrogen content of biogas and
COD reduction were 68% and 66%, respectively. In the final study, optimization of the
hydrogen production capability of the immobilized cells, including PEG concentration, cell
loading, curing times as well as effects of temperature and different inorganic components
concentrations on hydrogen production rate were studied. Result showed that with an
optimal PEG concentration (10 % w/v), cell loading (2.4 g dry wt.), curing time (80 min)
and inorganic components (NiCl
2
1 mg/L
,
FeCl
2
300 mg/L
removed
and MgSO
100 mg/L), attaining
an excellent hydrogen production rate of 7.3 L/L-POME/d and a hydrogen yield of 0.31 L
H
/g COD in continuous operation |
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