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1 of 16
Advisors
Dr. Christopher Sales
Jacob Price
REACTOR DESIGN TO TEST
HOW ALGAE PURIFIES
WASTEWATER
Group Members
Marina D’souza
Fatima Hasan
Section 940 – Group 14
1 of 16
OUTLINE
Background and motivation
 Algal blooms
 Harvesting algae
• High Density Bioreactor
Design aspect of project
 Technical activities
 Results
 Project timeline and budget 2 of 16
ALGAL BLOOMS
Nutrients such as nitrates
and phosphorus get into
water bodies.
Algae photosynthesize and
thus, remove the nutrients
from the water.
Algal blooms occur.
Algae can be harvested and
used for as fuel.
3 of 16
GROWING ALGAE
Membrane
bioreactors
Granular sludge
reactors
Biofilm reactors
4 of 16
HIGH DENSITY BIOREACTOR
5 of 16
Schematic of an HDBR (Figure adapted from Price et. al [1]
R – Reactor
BZ – Biomass Zone
PA – Pump A
A – Aerator
RT – Recycle Tank
PB – Pump B
FT – Influent/Feed
W – Waste Container
REACTOR 1
6 of 16
REACTOR 2
7 of 16
LIGHT SOURCE DESIGN
RGB LED light strip was used.
Pulse-width modulation (PWM)
is a technique used to modulate
the intensity of the lights.
An Arduino was used for digital
input
8 of 16
SAMPLING
9 of 16
20 mL
biomass
sample
1 mL
liquid
sample
HPLC
Wet biomass samples
RESULTS
10 of 16
1.500000
2.000000
2.500000
3.000000
3.500000
4.000000
4.500000
1 2 3 4
Biomass(g)
Condition
Biomass
R1 and R2 initial
R1 final
R2 final
RESULTS
NO3- -N
[mg -N / hr] [mg -N / hr / g biomass]
R^2
Uptake Rate Specific Uptake Rate
Reactor 1 Reactor 2 Reactor 1 Reactor 2 Reactor 1 Reactor 2
Condition 1 0.0615 0.0241 0.029661 0.012086 0.9373 0.6177
Condition 2 0.2251 0.0859 0.108563 0.043077 0.9157 0.6195
Condition 3 0.2389 0.0753 0.115655 0.038312 0.9802 0.5108
Condition 4 0.4503 0.0918 0.234772 0.044219 0.9262 0.4481
11 of 16
y = -0.0615x + 71.124
R² = 0.9373
y = -0.2251x + 110.84
R² = 0.9157
y = -0.2389x + 128.38
R² = 0.9802
y = -0.4503x + 201.42
R² = 0.9262
0
50
100
150
200
250
0 50 100 150 200
Mass(mgN)
Time (Hrs)
NO3- -N Reactor 1
C1
C2
C3
C4
Linear (C1)
Linear (C2)
Linear (C3)
Linear (C4)
RESULTS
12 of 16
1.500000
2.000000
2.500000
3.000000
3.500000
4.000000
4.500000
1 2 3 4
Biomass(g)
Condition
Biomass
R1 and R2 initial
R1 final
R2 final
RESULTS
NO3- -N
[mg -N / hr] [mg -N / hr / g biomass]
R^2
Uptake Rate Specific Uptake Rate
Reactor 1 Reactor 2 Reactor 1 Reactor 2 Reactor 1 Reactor 2
Condition 1 0.0615 0.0241 0.029661 0.012086 0.9373 0.6177
Condition 2 0.2251 0.0859 0.108563 0.043077 0.9157 0.6195
Condition 3 0.2389 0.0753 0.115655 0.038312 0.9802 0.5108
Condition 4 0.4503 0.0918 0.234772 0.044219 0.9262 0.4481
13 of 16
y = -0.0241x + 67.665
R² = 0.6177
y = -0.0859x + 119.42
R² = 0.6195
y = -0.0753x + 161.56
R² = 0.5108
y = -0.0918x + 269.77
R² = 0.4481
0
50
100
150
200
250
300
0 50 100 150 200
Mass(mgN)
Time (Hrs)
NO3- -N Reactor 2
C1
C2
C3
C4
Linear (C1)
Linear (C2)
Linear (C3)
Linear (C4)
PROJECT TIMELINE AND BUDGET
Week
Tasks 1 2 3 4 5 6 7 8 9 10
Literature study x x x
Reactor design and set up x x
Reactor testing x x x x x
Arduino system design and testing x x
Data analysis x x x
Final report preparation x x
14 of 16
Items Quantity Projected Cost ($)
Plastic tubes 2 15.14
LED lights 1 10.99
Arduino UNO 1 24.95
TP31 transistors 3 1.99
Breadboard 1 2.80
Jumper wires 15 1.95
12V Power adapter 1 4.99
5V Power adapter 1 4.76
Barrel Jack adapter 1 1.00
TOTAL 68.57
ANY QUESTIONS?
15 of 16
REFERENCES
1. J. Price, W. Shieh and C. Sales, "A Novel Bioreactor for High
Density Cultivation of Diverse Microbial Communities",
Journal of Visualized Experiments, no. 106, 2015.
2. T. Hirzel, “Arduino - PWM,” Arduino - PWM. [Online].
Available at: https://www.arduino.cc/en/tutorial/pwm.
[Accessed: 02-Apr-2016].
16 of 16

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engr103_grp94014_finPres

  • 1. Advisors Dr. Christopher Sales Jacob Price REACTOR DESIGN TO TEST HOW ALGAE PURIFIES WASTEWATER Group Members Marina D’souza Fatima Hasan Section 940 – Group 14 1 of 16
  • 2. OUTLINE Background and motivation  Algal blooms  Harvesting algae • High Density Bioreactor Design aspect of project  Technical activities  Results  Project timeline and budget 2 of 16
  • 3. ALGAL BLOOMS Nutrients such as nitrates and phosphorus get into water bodies. Algae photosynthesize and thus, remove the nutrients from the water. Algal blooms occur. Algae can be harvested and used for as fuel. 3 of 16
  • 5. HIGH DENSITY BIOREACTOR 5 of 16 Schematic of an HDBR (Figure adapted from Price et. al [1] R – Reactor BZ – Biomass Zone PA – Pump A A – Aerator RT – Recycle Tank PB – Pump B FT – Influent/Feed W – Waste Container
  • 8. LIGHT SOURCE DESIGN RGB LED light strip was used. Pulse-width modulation (PWM) is a technique used to modulate the intensity of the lights. An Arduino was used for digital input 8 of 16
  • 9. SAMPLING 9 of 16 20 mL biomass sample 1 mL liquid sample HPLC Wet biomass samples
  • 10. RESULTS 10 of 16 1.500000 2.000000 2.500000 3.000000 3.500000 4.000000 4.500000 1 2 3 4 Biomass(g) Condition Biomass R1 and R2 initial R1 final R2 final
  • 11. RESULTS NO3- -N [mg -N / hr] [mg -N / hr / g biomass] R^2 Uptake Rate Specific Uptake Rate Reactor 1 Reactor 2 Reactor 1 Reactor 2 Reactor 1 Reactor 2 Condition 1 0.0615 0.0241 0.029661 0.012086 0.9373 0.6177 Condition 2 0.2251 0.0859 0.108563 0.043077 0.9157 0.6195 Condition 3 0.2389 0.0753 0.115655 0.038312 0.9802 0.5108 Condition 4 0.4503 0.0918 0.234772 0.044219 0.9262 0.4481 11 of 16 y = -0.0615x + 71.124 R² = 0.9373 y = -0.2251x + 110.84 R² = 0.9157 y = -0.2389x + 128.38 R² = 0.9802 y = -0.4503x + 201.42 R² = 0.9262 0 50 100 150 200 250 0 50 100 150 200 Mass(mgN) Time (Hrs) NO3- -N Reactor 1 C1 C2 C3 C4 Linear (C1) Linear (C2) Linear (C3) Linear (C4)
  • 12. RESULTS 12 of 16 1.500000 2.000000 2.500000 3.000000 3.500000 4.000000 4.500000 1 2 3 4 Biomass(g) Condition Biomass R1 and R2 initial R1 final R2 final
  • 13. RESULTS NO3- -N [mg -N / hr] [mg -N / hr / g biomass] R^2 Uptake Rate Specific Uptake Rate Reactor 1 Reactor 2 Reactor 1 Reactor 2 Reactor 1 Reactor 2 Condition 1 0.0615 0.0241 0.029661 0.012086 0.9373 0.6177 Condition 2 0.2251 0.0859 0.108563 0.043077 0.9157 0.6195 Condition 3 0.2389 0.0753 0.115655 0.038312 0.9802 0.5108 Condition 4 0.4503 0.0918 0.234772 0.044219 0.9262 0.4481 13 of 16 y = -0.0241x + 67.665 R² = 0.6177 y = -0.0859x + 119.42 R² = 0.6195 y = -0.0753x + 161.56 R² = 0.5108 y = -0.0918x + 269.77 R² = 0.4481 0 50 100 150 200 250 300 0 50 100 150 200 Mass(mgN) Time (Hrs) NO3- -N Reactor 2 C1 C2 C3 C4 Linear (C1) Linear (C2) Linear (C3) Linear (C4)
  • 14. PROJECT TIMELINE AND BUDGET Week Tasks 1 2 3 4 5 6 7 8 9 10 Literature study x x x Reactor design and set up x x Reactor testing x x x x x Arduino system design and testing x x Data analysis x x x Final report preparation x x 14 of 16 Items Quantity Projected Cost ($) Plastic tubes 2 15.14 LED lights 1 10.99 Arduino UNO 1 24.95 TP31 transistors 3 1.99 Breadboard 1 2.80 Jumper wires 15 1.95 12V Power adapter 1 4.99 5V Power adapter 1 4.76 Barrel Jack adapter 1 1.00 TOTAL 68.57
  • 16. REFERENCES 1. J. Price, W. Shieh and C. Sales, "A Novel Bioreactor for High Density Cultivation of Diverse Microbial Communities", Journal of Visualized Experiments, no. 106, 2015. 2. T. Hirzel, “Arduino - PWM,” Arduino - PWM. [Online]. Available at: https://www.arduino.cc/en/tutorial/pwm. [Accessed: 02-Apr-2016]. 16 of 16

Editor's Notes

  1. Image taken from http://www.sea-way.org/blog/Qingdao_algae_bloom01.JPG
  2. Images taken from http://www.aiche.org/sites/default/files/styles/chenected_lead_image/public/images/Chenected/lead/rab.jpg?itok=HbniKxV_ http://g04.s.alicdn.com/kf/HTB1og5WFFXXXXXUapXXq6xXFXXXc/220758633/HTB1og5WFFXXXXXUapXXq6xXFXXXc.jpg http://4.bp.blogspot.com/-5u9d0ep0gt8/TXFPoE_kC6I/AAAAAAAAAD4/fM2eTqRxzMw/s1600/uasb-scheme.gif
  3. A type of biofilm reactor was adapted by Dr. Sales and his team of researchers to cultivate algae. This novel design is called the High Density Bioreactor.