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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
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
INTRODUCTION: PHOTOBIOREACTOR
Arthrospira production plant in Calipatria, California
Source: Mostafa 2012
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).
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
INTRODUCTION: Bti TOXIN
Mode of action for Bt toxin crystal
Source: Jurat-Fuentes
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
 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
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
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)
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
082003300390
10002100260380
CBCAB
CBAoductivity
...
....Pr


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
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

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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
  • 3. INTRODUCTION: PHOTOBIOREACTOR Arthrospira production plant in Calipatria, California Source: Mostafa 2012
  • 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
  • 6. INTRODUCTION: Bti TOXIN Mode of action for Bt toxin crystal Source: Jurat-Fuentes
  • 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 082003300390 10002100260380 CBCAB CBAoductivity ... ....Pr  
  • 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