Photobioreactor Review: Controlling malaria vector with Anabaena sp. strain PCC 7120 based a study by Ketseoglou & Bouwer. An optimization on the volumetric productivity was performed based on three factors described by the authors. This presentation serves just as a review for the authors' work but for education purpose only. All credit are due to the authors of the journal at http://www.sciencedirect.com/science/article/pii/S0168165613002381
Controlling malaria vector with Anabaena sp. strain PCC 7120
1. KKKB 5933: ADVANCED BIOREACTOR ENGINEERING
BERNARD CHUNG KEN VUI
A98753
KB/4
Controlling malaria vector with
Anabaena sp. strain PCC 7120:
A study by Ketseoglou & Bouwer
2. INTRODUCTION: PHOTOBIOREACTOR
Photobioreactor: specialized bioreactor that uses phototropic
microorganisms to generate bioproducts by using light as the main
energy source (Kunjapur & Eldridge 2010)
Either in an open cultivation system (pond) or in the closed cultivation
system (Ketseoglou & Bouwer 2013)
Closed systems include:
A) Flat plate
B) Bubble column
C)Tubular
Source: Posten 2009
Potential bioproducts from phototropic microorganisms: Astaxanthin,
β-carotene, phycobiliproteins, biodiesel, jet fuel, and biofertilizer
4. INTRODUCTION: MALARIA
Malaria: An insect-transmitted disease
that remains one of the greatest global
health challenges of the modern era
(Oliva et al. 2013).
Caused by Plasmodium falciparum
(parasite) and is transmitted by a bite
from an infected female Anopheles
mosquito (Janneck et al. 2011).
The new technology to develop a
better insecticide has bring the
attention of using genetically
engineered cyanobacteria as
biopesticides for the control of
mosquitoes (Ketseoglou & Bouwer
2013).
5. INTRODUCTION: Bti TOXIN
Biopesticide uses the highly toxic crystalline inclusions
produced by Bacillus thuringiensis subspecies israelensis (Bti)
Endotoxin protein produced by Bti is commonly known as the
crystal protein (Cry) through Cry gene
Disadvantages (Ketseoglou & Bouwer 2013):
Possess low persistence in the field (inactivation by
ultraviolet)
Problem due to ingestion by other aquatic organisms
Settling from the mosquito larval feeding zone
7. CASE STUDY: OBJECTIVE
Optimization of photobioreactor growth conditions for a
cyanobacterium expressing mosquitocidal Bacillus thuringiensis
Cry proteins
By: Irene Ketseoglou, Gustav Bouwer
Link: http://www.sciencedirect.com/science/article/pii/S0168165613002381
Cyanobacterium Anabaena sp. strain PCC 7120 has been genetically
engineered to express important Cry genes such as cry4Aa, cry11Aa
and p20
Objective: To determine the optimal growth conditions for PCC
7120#11 in an indoor, flat-plate photobioreactor using RSM
8. Cultivation of PCC 7120#11 till it reaches mid-exponential growth
Introduced into the photobioreactor at initial cell concentration of
1.6 x 106 cells mL-1
Experimental Designs:
Flat-plate, inclined modular photobioreactor with two
toughened glass plates (6 mm thick, 702 mm length and 516 mm
height)
Medium used: 3.7 L BG-11 for algae
Temperature: 30 °C
pH: 7.2
Continuous illumination: 58 μmol m-2 s-1 with a panel of 8 Grolux
lamp
Constant agitation: 140 rpm carbon dioxide-enriched air-bubble
mixing system
Factors such as airflow, photosynthetic photon flux density (PPFD),
and CO2 affect the growth and development of cyanobacteria
Response is on the volumetric productivity of PCC
CASE STUDY: METHOD
9. CASE STUDY: FINDINGS
Effect of input CO2 concentration and airflow rate at low
PPFD (53.0 μmol m-2 s-1) on the volumetric productivity
10. CASE STUDY: FINDINGS
Effect of airflow rate and PPFD on PCC 7120#11 volumetric productivity
at a input CO2 concentration of 3.75% (v/v)
11. CASE STUDY: FINDINGS
1. Prediction equation:
2. Numerical optimization reveals that the highest volumetric
productivity of 0.47 g L−1 d−1 were predicted to be a PPFD of 154
μmol m−2 s−1, an airflow rate of 1.02 vvm and an input CO2
concentration of 3.18 % (v/v).
3. For commercialization where cost of production is the main
objective, numerical optimization reveals that optimal volumetric
productivity of 0.44 g L−1 d−1 were obtained at a PPFD of 139.66
μmol m−2 s−1, an airflow rate of 1.00 vvm and an input CO2
concentration of 1.50 % (v/v)
4. Larvicidal activity: Mean of LC50 as reported for the runs was 9.24 x
105 cells mL-1
2
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CBCAB
CBAoductivity
...
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12. CASE STUDY: CONCLUSIONS
Source Ketseoglou &
Bouwer 2013
Yoon et al. 2008 Fontes et al.
1987
Yu et al. 2011
Type of
photobioreactor
Flat-plate Bubble
(Annular)
Airlift Airlift
Parameters
studied
PPFD, CO2 input,
Airflow rate
Superficial gas
velocity, pH,
Initial
phosphate
concentration,
Light intensity
Airflow rate,
Light density
Mixotrophic
culture
Productivity 0.47 g L−1 d−1
(maximum)
0.44 g L−1 d−1
(optimum)
0.67 g L−1 d−1
(optimum)
13 g m−2 d−1
(optimum)
0.43 g L−1 d−1
(optimum)
Comparisons of different findings on the characterization and design studies
13. THE FUTURE
1. Future PCC 7120#11 studies may want to determine if volumetric
productivity has an impact on the ratio of the LC50 of late-
exponential phase cells to the LC50 of mid-exponential phase cells.
2. A comparison of the different studies suggests that PCC 7120 may
have a lower volumetric productivity maximum than other
cyanobacteria
3. Provide a foundation for future continuous culture optimization
experiments, in which key process parameters are monitored and
controlled on a continual basis
4. Extensive scale-up studies are necessary to evaluate the feasibility
of commercial-scale production of PCC 7120#11