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Redesign of a Partitioned
Aquaculture System
Austin Bartley
Kayla Kernich
Emily Skibenes
Introduction
https://www.facebook.com/allaboutalgae/photos/a.371644646330812.1073741825.371642179664392/371645722997371/?typ
e=3&theater
What is a Partitioned Aquaculture System?
Developed at Clemson University in
1989, the partitioned aquaculture
system (PAS) was designed to optimize
fish production in pond systems by
increasing net oxygen production
through the management of algal
productivity
Schematic of Partitioned Aquaculture System at Clemson University
http://www.sciencedirect.com/science/article/pii/S014486099900028X#FIG1
Why a Partitioned Aquaculture System?
โ— Major advantages of pond fish culture:
โ—‹ Low capital cost of earthen ponds
โ—‹ Reliability of pond fish production
โ— Disadvantages of pond fish culture:
โ—‹ Need to continuously manage pond oxygen concentration
โ—‹ Need to continuously manage other fluctuating water quality variables
โ— These management difficulties, combined with land, water, and environmental
constraints, have driven the search for technological improvements in pond
aquaculture
What is a Partitioned Aquaculture System?
http://www.lsuagcenter.com/portals/communications/publications/agmag/
archive/1999/fall/potential-for-the-partitioned-aquaculture-system-in-
louisiana
The most significant difference between
conventional pond aquaculture and the PAS is
that the PAS achieves high algal yields by
maintaining uniform water velocities
The optimization of algal production allows for an
increase in fish carrying capacity.
PAS Utilization for Production of Algae and Carbon Capture
โ— Algae transform carbon dioxide into biomass
and oxygen during photosynthesis
โ— Algae help in mitigating the effects of global
climate change by capturing CO2 from the
earth's atmosphere
โ— Algal biomass is used in various industries:
โ—‹ Nutraceutical
โ—‹ Cosmetic
โ—‹ Pharmaceutical
โ—‹ Bioenergy applications
Photo by Emily Skibenes
PAS Utilization for Production of Algae and Carbon Capture
โ— Algal raceways ponds are
commonly used in the
commercial production of
algal biomass
โ— Advantages:
โ—‹ Simple design
โ—‹ Low capital and operating
costs
โ—‹ Easy to construct and
operate
โ— PAS can be operated for
algal biomass production
instead of fish farming
Conventional Algal Raceway Ponds
http://www.sciencedirect.com/science/article/pii/S096014811300342X#bib12
Recognition & Definition of Problem
โ— Original Partitioned
Aquaculture System (PAS)
unit is scheduled to be
decommissioned in the near
future
โ— Removal of PAS hinders the
ability to conduct class
projects and research
โ— New system to be relocated
near the Student Organic
Farm
Photo by Emily Skibenes
2010 qPublic.net
http://qpublic5.qpublic.net/qpmap4/map_sc_pickens.php?county=sc_pickens&layers=roads+topos
Goals
Biological:
โ— Carbon sequestration by algal
growth
โ—‹ 10 g C/m2/day
โ— Determining required nutrient
concentrations
โ— Sustaining water quality
โ— Maximize biomass yield
Structural:
โ— Raceways allowing for desired
cell retention time
โ—‹ 1 - 3 days
โ— Raceways allowing for desired
water velocity in channel
โ—‹ 0.125 m/s
โ— Integrity of system
โ— Safety
โ— Aesthetics
Goals
Mechanical:
โ— Water access
โ— Water movement
โ— Algae harvesting
โ— Water level control
Educational:
โ— Use as tool for students and
visitors
Constraints & Considerations
โ— Constraints
โ—‹ Limited monetary resources for
building/design
โ—‹ Area of land limits possible
configurations and orientations
โ—‹ Water sources in the area
limited and distant from PAS
location
โ—‹ Location floods often
โ— Considerations
โ—‹ Safety of working/walking around the
system.
โ–  Fence/height of structure prevents
children and animals from falling into
system
โ—‹ Ecological impact
โ—‹ Compensate for evaporative water loss
โ—‹ Ethical
3 Questions:
User: Biosystems Engineering faculty/students
How often does algae need to be harvested?
How often/how much nutrients need to be added to the system?
What maintenance will be required?
Can this system be altered to allow for fish cultivation?
Client: Ag. Department
What are the upfront costs of installation (piping, pump, concrete, etc)?
What are the operating costs?
What future research can come from this system?
Design team:
What is the most efficient way to capture the algae?
What water velocity in the channel will produce the highest yield of algae?
What cell retention time would meet our carbon productivity goal?
Literature Review
https://www.facebook.com/allaboutalgae/photos/a.371644646330812.1073741825.371642179664392/371645722997371/?typ
e=3&theater
Past Experience/Heuristics
โ— Creative inquiry to replace paddle wheel design
โ— Experience working with and around the PAS
โ— Creative inquiry on aquaculture at student organic farm
โ— Co-op experience at Harper Corporation
โ— Dr. Murdochโ€™s Hydrogeology class on wells
โ— Relevant Course curriculum for various parts of PAS design
โ—‹ CE 3410: Fluid Mechanics
โ—‹ BE 4100 : Biological Kinetics
โ—‹ BE 4120: Heat and Mass Transfer
โ—‹ CE 2060: Structural Mechanics
Governing Equations:
โ— Mass balance at steady state
โ—‹ (QC/V) - (QC/V) +/- r = 0
โ— Specific Growth Rate (Haldane light-inhibited model)
โ—‹ ฮผL=ฮผmaxIL/KL+IL+IL
2/Ki
โ— Algal Photosynthesis:
โ—‹ 106 CO2 + 16 NO3
- + HPO4
2- + 122 H2O +18H+ = C106 H152 O53 N16 P + 106 02 +
138O2
Governing Equations:
โ— Reynolds Number
โ—‹ Re = ฯudh/ฮผ
โ— Bernoulliโ€™s Equation
โ—‹ h0 + P0/ฯg + V0^2/2g + ฮ”hp = h1 + P1/ฯg + V1^2/2g + ฮ”hf + ฮ”hm
โ— Energy equation
โ—‹ P1โ€‹โ€‹+โ€‹1/2ฯv1
2โ€‹โ€‹+ฯgh1โ€‹โ€‹=P1โ€‹โ€‹+โ€‹1/2ฯvโ€‹2
โ€‹2โ€‹โ€‹+ฯgh2โ€‹โ€‹
โ— Pump Flow Rate
โ—‹ Qg/Qw = [โดwgL/P2ln(P0/P2)]
Possible Options to Address Problem
Water Source:
โ— Hunnicutt Creek
โ— Seneca River
โ— Well water
โ— Municipal water from Organic Farm
โ— Rain barrels
Algae Capture:
โ— Centrifugation
โ— Flocculation
โ— Physical Separation
โ—‹ Sedimentation
โ—‹ Filtration
PAS Elevation:
โ— Above ground
โ— Below ground
โ— Other levels
Outflow Water Handling:
โ— Pump into well source
โ— Pump into storage tank
โ— Pump straight back into system
Mechanical Flow Device:
โ— Paddlewheel
โ— Air lift pump
Hard Data from Literature
โ— Cell Retention Time for Algae Growth
โ—‹ ๐œ = 1.2 and 2.5 days
โ— Culture Depth
โ—‹ d = 0.3 m and 0.61 m
โ— Water Velocity
โ—‹ v = 0.031, 0.062, and 0.125 m/s
The partitioned aquaculture system: impact of design and environmental parameters on
algal productivity and photosynthetic oxygen production. Drapcho, C., Brune, D. (2000)
โ— Algal Productivity Rate
โ—‹ 5 - 10 g C/m2/d
โ— External Inorganic Carbon Addition
Rates
โ—‹ 0, 0.6, and 1.2 mmol/L/day
Data from Field Work:
โ— Water level in Dr. Murdochโ€™s well after
heavy rainfall: 1.33 m
โ— Using surveying equipment, elevation
difference from site to well: (1.99 m -
1.58 m): 0.41 m
โ— Theoretical water level at site: 0.92 m
Photo by Emily Skibenes
Design Methodology & Materials
https://www.facebook.com/allaboutalgae/photos/a.371644646330812.1073741825.371642179664392/371645722997371/?typ
e=3&theater
Analysis of Information
Length: 15.19 m
Width: 28.35 m
Depth: 0.61 m
SA: 375.37 m2
V: 228.825 m3 or 228,824.6 L
*See appendix for calculations
Synthesis of Design - Advantages and Disadvantages of
Culture Depth
Culture depth: 0.25 to 0.34 m
Advantages:
โ— Biomass concentration is higher
Disadvantages:
โ— Greater temperature fluctuation
โ—‹ Water Temperature
Fluctuations (Morning -> Mid
afternoon, May - September)
โ–  ฮ”T = 12.6 ยฐF (for d = 0.30 m)
โ–  ฮ”T = 5.4 ยฐF (for d = 0.61 m)
Culture depth: 0.34 m to 0.61 m
Advantages:
โ— Easier and less expensive to
mix
Design culture depth = 0.61 m
Water Volume Calculations
Assuming water evaporates from the surface1 at 0.5 cm/day:
Water loss due to evaporation: 1.88 m3/day or 1876.84 L/day
Assuming Clemsonโ€™s average annual precipitation2: 127.36 cm/yr:
Water gain due to rainfall: 1.31 m3/day or 1309.73 L/day
Change in water per day:
ฮ” = -567.11 L/day = -0.567 m3/day
Water Quality Results
Samples from Hunnicutt Creek,
Seneca River, and a well near the plot
of land were tested. Desired water
quality parameters were met for all 3
sources.
Therefore, we decided to use
economics and logistics as our main
criteria for choosing water source.
Image from Google Maps
Cost Analysis of Water Sources
Seneca River: $6,640.00
โ— Includes pipe installation for 280.0 m and 2 HP pump
Hunnicutt Creek: $11,320.00
โ— Includes pipe installation for 516.1 m and 2 HP pump
Well water: $7,015.00
โ— Less variability in water quality, and less disturbance of surrounding area
Municipal water: $1,200.00
โ— Includes pipe installation for 57.6 m
Drilling a Well
Total Price: $7,015.00
Item Description Price
6โ€™โ€™ drilled well: 30โ€™ @ $12/ft $3600.00
6โ€™โ€™ PVC casing: 70โ€™ @ $5/ft $350.00
Bentonite Grout $150.00
Well Seal $25.00
Permit $70.00
ยพ HP 10gal/min Schaefer Submersible Pump $1,100.00
260 ft 1โ€™โ€™ Schedule 80 Pipe and 12/3 Pump Wire in Well $520.00
PC144 44 gal tank, pressure switch, gauge, and misc. fittings $700
Ditch, Pipe, and Wire to system $350
Breaker and wire from tank to electrical panel $50
Small Rock Cover $100
Algae & Inoculation
โ— Chlorella vulgaris
โ— Common green algae
โ— Matches or is close to algae used in
reference literature
โ— Valuable bioproducts
Chlorella vulgaris
https://botany.natur.cuni.cz/algo/database/node/110
Algae & Inoculation
Steps to inoculate PAS units:
1. Receive flask stock culture
2. Transfer to 500-1000 mL beakers
a. with Boldโ€™s Basal medium
3. Transfer to 19 L bottles
a. At least 0.5 g/L cell concentration
4. Three 19 L bottles per unit
a. Allow 4 - 6 weeks for peak biomass
Flow Diagram
Sketch by Emily
Mass Balance Schematic of CSTR with Internal Cell Recycle
Mass Balance Approach for CSTR w/ Recycle
โ— Utilizing mass balances and
Monod kinetics
โ—‹ Determine whether system
needs external inorganic
carbon inputs to achieve
goal of 10 g C/m2/day
Mass balance and Monod kinetic equations used
in Excel
Mass Balance Approach for CSTR w/ Recycle
โ— No addition of external inorganic carbon needed for system
Cell Retention Time (ฮ˜) (hr) 48
Hydraulic Retention Time (ฯ„) (hr-1) 14.75
Specific Growth Rate (ฮผ) (hr-1) 0.023
Rate of Biomass Formation (rXB) (g/m2/day) 27.99
Rate of Carbon Productivity (rS) (g/m2/day) 10.03
Nutrient Addition
Nutrient g/unit/week g/system/week
Nitrogen 518.00 2072.00
Phosphorus 160.00 640.00
Synthesis of Design: Degree of Mixing
Mixing in an open raceway may increase algal productivity by:
โ— Increasing the exposure of the algal cells to sunlight
โ— Enhance vertical mixing
โ— Preventing cell settling
โ— Prevent thermal stratification
2 options assessed to achieve design flow of 0.125 m/s: (1) air lift pump; (2)
paddlewheel
Air Lift Pump
Source: Effortless Aquaponics
pressure
โ— Estimated cost:
$2,900.00
โ— Testing and research
needed to determine if
desired flow for
operating conditions
can be achieved.
Paddlewheels
Paddlewheels are the traditional and
most commonly used method of flow
and mixing
Uniform water velocities can easily be
achieved with the use of low rpm (1- to
3-rpm) paddlewheels
Pentair Paddlewheel Assembly
(PW11-AQ)
Cost per unit: $1,112.00
Total cost for system: $4,448.00
Algae Separation
โ— 1 x 3.5 m belt
โ— Duck cloth or canvas
belt
โ— 4 rpm or 3.8 cm/s
โ— Harvest every 7 days
โ— Frame 1.1 x 1.2 x 1.5 m
Source: Iowa State University
Algae Separation Cost Analysis
โ— Motor - $300.00 each
โ— Rollers - $345.00 per roller, $1,035.00 per unit
โ— Belt - $100.00 each
โ— Frame - $210.00 steel angle iron
โ— Other - $150.00 paint, feet, and fittings
โ— Total - $1795.00 per unit, $7,180.00 total
Instrumentation
Schematic
Instrumentation
Campbell Scientific AquaOne plus AquaBuoy
System
โ— Performs automated monitoring, control, and
alarm functions in recirculating, flow-through,
and open-pond aquaculture.
โ— Designed to measure input from water-quality,
flow, and amp sensors, and control aerators,
pumps, alarms, and communication devices.
โ— Almost any sensor can be used, including
dissolved oxygen, temperature, pH, conductivity,
salinity, turbidity, ORP, ammonia, flow, and level Price: $1,495.00
Fencing
Simple fence estimated at:
โ— 4 ft. T - post, 71 units: $260.00
โ— Welded wire, 4 x 100 ft., 4 rolls:
$280.00
โ— Amethyst Falls Wisteria, 17 plants:
$255.00
โ— Blackberry bush, 28 plants: $205.00
โ— Total: $1,000.00
โ— Total w/ 10% labor: $1,100.00
Amethyst Falls Wisteria
Source: www.theplantingtree.com
Ground Cover
Ground cover to solve problem of mowing: 1 ft of gravel estimated at:
โ— Recycled 57 stone: ($16/ton)(1.21 ton/yd3)(128.718 yd3)(โ…”) = $1661.32
โ— Recycled crusher run: ($10/ton)(2 ton/yd3)(128.718 yd3)(โ…“) = $858.12
โ— Total: $2519.43
โ— Total w/ 20% labor & delivery: $3023.00
Sustainability Measures
โ— Recycling water from PAS
โ— Carbon capture by algae
โ— Potential for creation of
sustainable materials
โ— Educational aspect
Budget:
Total cost of implementation:
$144,186.23
Concrete: $101,470.43
Paddlewheel: $4,448.00
Well Installation: $7,015.00
Algae Capture System: $7,180.00
Instrumentation: $1,495.00
Ground Cover: $3,023.00
Fencing: $1,100.00
Budget - Operating Costs
Description Energy Usage (kW-hr/day)
Paddlewheel 17.88
Inflow Pumps (2 EA) 1.024
Algae Collectors 14.32
Total Energy Usage 33.22
Solar array required: 10kW system
Total System Cost: $18,454.80
Area Requirement: 600 ft2
Conclusions:
Water Source:
โ— Well water to operate PAS
Algae Capture:
โ— Mechanical belt system
Nutrient Addition:
โ— No external inorganic carbon
needed to achieve goal
โ— Add 2072.00 g N/week and
640.00 g P/week
PAS Elevation:
โ— 2 ft deep
โ— 2 ft above ground
Mechanical Flow Device:
โ— Paddlewheel to achieve 0.125 m/s
flow velocity
3 Questions of the User: BE faculty/students
1. How often does algae need to be harvested?
โ— Approximately every 7 days
1. How often/how much nutrient needs to be added to the system?
โ— Weekly addition of 2072 g Nitrogen and 640 g Phosphorous
1. What maintenance will be required?
โ— Weekly maintenance is required to remove the algae, the water parameters are
all monitored by sensors continuously. PAS will need to be maintained at the
beginning of each May (growing season)
1. Can this system be altered to allow for fish cultivation?
โ— Yes, by removing the algae capturing device and adding additional fish feed, fish
can be added
3 Questions of the Client: Ag. Department
1. What are the upfront costs of installation (piping, pump, concrete, etc)?
โ— Total overall cost: $145,690.89
1. What are the operating costs?
โ— Dependent on energy source used
1. What future research can come from this system?
โ— Adding a greenhouse for seasonal extension
โ— Operating the system with fish or other aquatic organisms
โ— Testing varying algal capturing mechanisms for max algal yield
โ— Determining possibilities of air lift pumps for forced flow
3 Questions of the Design Team:
1. What is the most efficient way to capture the algae?
โ— For our system, mechanical belt system
1. What water velocity in the channel will produce the highest yield of algae?
โ— During the day: 0.125 m/s
1. What cell retention time would meet our carbon productivity goal?
โ— 48 hours
Timeline
References/Patents
1. Brune, D., et al. (2004).19 Partitioned Aquaculture Systems: Biology and Culture of Channel Catfish Developments
in Aquaculture and Fisheries Science pp. 561โ€“584., https://doi.org/10.1016/s0167-9309(04)80021-8.
2. Caswell, W.; Norvell, K. (2016) Algal harvesting in the Partitioned Aquaculture System: Clemson University, BE
4750 Senior Design
3. Chisti Y. (2016). Large-Scale Production of Algal Biomass: Raceway Ponds: Algae Biotechnology pp 21-40.
https://doi.org/10.1007/978-3-319-12334-9_2
4. Clark, N, Dabolt, R. (1986) A General Design Equation for Air Lift Pumps Operating in Slug Flow: AiChE Journal
pp 56-64. doi: 10.1002/aic.690320107
5. Drapcho, C., Brune, D. (2000). The partitioned aquaculture system: Impact of design and environmental
parameters on algal productivity and photosynthetic oxygen production: Aquacultural Engineering. 21. 151-168.
https://doi.org/10.1016/S0144-8609(99)00028-X
References/Patents
6. Gross, M
7. Mandal S, Mallick N. Biodiesel Production by the Green Microalga Scenedesmus obliquus in a Recirculatory
Aquaculture System: Applied and Environmental Microbiology. 2012;78(16):5929-5934. doi:10.1128/AEM.00610-
12.
8. Swann, L. A Fish Farmerโ€™s Guide to Understanding Water Quality: Illinois-Indiana Sea Grant Program Purdue
University
9. Turker, H., Eversole, A., Brune, D. (2003). Filtration of green algae and Cyanobacteria by Nile tilapia,
Oreochromis niloticus, in the Partitioned Aquaculture System: Aquaculture. 215. 93-101.
https://doi.org/10.1016/S0044-8486(02)00133-3.
10. Wurts, W, McNeill, S, Overhults, D. (1994). Performance and Design Characteristics of Airlift Pumps for Field
Applications: World Aquaculture: 25(4): 51-55. http://www2.ca.uky.edu/wkrec/AirliftPumps.htm
Appendices - Volume Calculations
Appendices - Structural Calculations
Appendices - Water Quality Test (Hunnicutt)
Appendices - Water Quality Test (Seneca River)
Appendices - Water Quality Test (Well Water)
Appendices - Soil Test
Appendices - Design Calculations
Appendices - Air Lift Pump Equations
โ— Solving for Velocity:
โ—‹ Vg= Vw * [โดwgL/P2ln(P0/P2)] *
โ—‹ L = 0.05 m
โ—‹ P2 = 101 kPa = 101,000 kg/m*s2
โ—‹ P0 = P2 + โดwgh = 106,000 kg/m*s2
โ—‹ g = 9.81 m/s2
โ—‹ โดw = 1000 kg/m3
โ—‹ Vw = Velocity of effluent water (m/s)
โ—‹ Vg = Velocity of injected gas (m/s)
Appendices - Air Lift Pump Equations (Cont.)
โ— Modified Bernoulliโ€™s equation:
โ—‹ แน0(V0
2/2g + h0) + แน1(V1
2/2g + h1) = แน2(V2
2/2g + h2) + ฮ”hf
โ—‹ แน = mass flow rate (kg/s)
โ—‹ V = velocity (m/s)
โ—‹ g = 9.81 m/s2
โ—‹ h = height (m)
โ—‹ ฮ”hf = friction loss (m)

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New pas design final presentation

  • 1. Redesign of a Partitioned Aquaculture System Austin Bartley Kayla Kernich Emily Skibenes
  • 3. What is a Partitioned Aquaculture System? Developed at Clemson University in 1989, the partitioned aquaculture system (PAS) was designed to optimize fish production in pond systems by increasing net oxygen production through the management of algal productivity Schematic of Partitioned Aquaculture System at Clemson University http://www.sciencedirect.com/science/article/pii/S014486099900028X#FIG1
  • 4. Why a Partitioned Aquaculture System? โ— Major advantages of pond fish culture: โ—‹ Low capital cost of earthen ponds โ—‹ Reliability of pond fish production โ— Disadvantages of pond fish culture: โ—‹ Need to continuously manage pond oxygen concentration โ—‹ Need to continuously manage other fluctuating water quality variables โ— These management difficulties, combined with land, water, and environmental constraints, have driven the search for technological improvements in pond aquaculture
  • 5. What is a Partitioned Aquaculture System? http://www.lsuagcenter.com/portals/communications/publications/agmag/ archive/1999/fall/potential-for-the-partitioned-aquaculture-system-in- louisiana The most significant difference between conventional pond aquaculture and the PAS is that the PAS achieves high algal yields by maintaining uniform water velocities The optimization of algal production allows for an increase in fish carrying capacity.
  • 6. PAS Utilization for Production of Algae and Carbon Capture โ— Algae transform carbon dioxide into biomass and oxygen during photosynthesis โ— Algae help in mitigating the effects of global climate change by capturing CO2 from the earth's atmosphere โ— Algal biomass is used in various industries: โ—‹ Nutraceutical โ—‹ Cosmetic โ—‹ Pharmaceutical โ—‹ Bioenergy applications Photo by Emily Skibenes
  • 7. PAS Utilization for Production of Algae and Carbon Capture โ— Algal raceways ponds are commonly used in the commercial production of algal biomass โ— Advantages: โ—‹ Simple design โ—‹ Low capital and operating costs โ—‹ Easy to construct and operate โ— PAS can be operated for algal biomass production instead of fish farming Conventional Algal Raceway Ponds http://www.sciencedirect.com/science/article/pii/S096014811300342X#bib12
  • 8. Recognition & Definition of Problem โ— Original Partitioned Aquaculture System (PAS) unit is scheduled to be decommissioned in the near future โ— Removal of PAS hinders the ability to conduct class projects and research โ— New system to be relocated near the Student Organic Farm Photo by Emily Skibenes
  • 10. Goals Biological: โ— Carbon sequestration by algal growth โ—‹ 10 g C/m2/day โ— Determining required nutrient concentrations โ— Sustaining water quality โ— Maximize biomass yield Structural: โ— Raceways allowing for desired cell retention time โ—‹ 1 - 3 days โ— Raceways allowing for desired water velocity in channel โ—‹ 0.125 m/s โ— Integrity of system โ— Safety โ— Aesthetics
  • 11. Goals Mechanical: โ— Water access โ— Water movement โ— Algae harvesting โ— Water level control Educational: โ— Use as tool for students and visitors
  • 12. Constraints & Considerations โ— Constraints โ—‹ Limited monetary resources for building/design โ—‹ Area of land limits possible configurations and orientations โ—‹ Water sources in the area limited and distant from PAS location โ—‹ Location floods often โ— Considerations โ—‹ Safety of working/walking around the system. โ–  Fence/height of structure prevents children and animals from falling into system โ—‹ Ecological impact โ—‹ Compensate for evaporative water loss โ—‹ Ethical
  • 13. 3 Questions: User: Biosystems Engineering faculty/students How often does algae need to be harvested? How often/how much nutrients need to be added to the system? What maintenance will be required? Can this system be altered to allow for fish cultivation? Client: Ag. Department What are the upfront costs of installation (piping, pump, concrete, etc)? What are the operating costs? What future research can come from this system? Design team: What is the most efficient way to capture the algae? What water velocity in the channel will produce the highest yield of algae? What cell retention time would meet our carbon productivity goal?
  • 15. Past Experience/Heuristics โ— Creative inquiry to replace paddle wheel design โ— Experience working with and around the PAS โ— Creative inquiry on aquaculture at student organic farm โ— Co-op experience at Harper Corporation โ— Dr. Murdochโ€™s Hydrogeology class on wells โ— Relevant Course curriculum for various parts of PAS design โ—‹ CE 3410: Fluid Mechanics โ—‹ BE 4100 : Biological Kinetics โ—‹ BE 4120: Heat and Mass Transfer โ—‹ CE 2060: Structural Mechanics
  • 16. Governing Equations: โ— Mass balance at steady state โ—‹ (QC/V) - (QC/V) +/- r = 0 โ— Specific Growth Rate (Haldane light-inhibited model) โ—‹ ฮผL=ฮผmaxIL/KL+IL+IL 2/Ki โ— Algal Photosynthesis: โ—‹ 106 CO2 + 16 NO3 - + HPO4 2- + 122 H2O +18H+ = C106 H152 O53 N16 P + 106 02 + 138O2
  • 17. Governing Equations: โ— Reynolds Number โ—‹ Re = ฯudh/ฮผ โ— Bernoulliโ€™s Equation โ—‹ h0 + P0/ฯg + V0^2/2g + ฮ”hp = h1 + P1/ฯg + V1^2/2g + ฮ”hf + ฮ”hm โ— Energy equation โ—‹ P1โ€‹โ€‹+โ€‹1/2ฯv1 2โ€‹โ€‹+ฯgh1โ€‹โ€‹=P1โ€‹โ€‹+โ€‹1/2ฯvโ€‹2 โ€‹2โ€‹โ€‹+ฯgh2โ€‹โ€‹ โ— Pump Flow Rate โ—‹ Qg/Qw = [โดwgL/P2ln(P0/P2)]
  • 18. Possible Options to Address Problem Water Source: โ— Hunnicutt Creek โ— Seneca River โ— Well water โ— Municipal water from Organic Farm โ— Rain barrels Algae Capture: โ— Centrifugation โ— Flocculation โ— Physical Separation โ—‹ Sedimentation โ—‹ Filtration PAS Elevation: โ— Above ground โ— Below ground โ— Other levels Outflow Water Handling: โ— Pump into well source โ— Pump into storage tank โ— Pump straight back into system Mechanical Flow Device: โ— Paddlewheel โ— Air lift pump
  • 19. Hard Data from Literature โ— Cell Retention Time for Algae Growth โ—‹ ๐œ = 1.2 and 2.5 days โ— Culture Depth โ—‹ d = 0.3 m and 0.61 m โ— Water Velocity โ—‹ v = 0.031, 0.062, and 0.125 m/s The partitioned aquaculture system: impact of design and environmental parameters on algal productivity and photosynthetic oxygen production. Drapcho, C., Brune, D. (2000) โ— Algal Productivity Rate โ—‹ 5 - 10 g C/m2/d โ— External Inorganic Carbon Addition Rates โ—‹ 0, 0.6, and 1.2 mmol/L/day
  • 20. Data from Field Work: โ— Water level in Dr. Murdochโ€™s well after heavy rainfall: 1.33 m โ— Using surveying equipment, elevation difference from site to well: (1.99 m - 1.58 m): 0.41 m โ— Theoretical water level at site: 0.92 m Photo by Emily Skibenes
  • 21. Design Methodology & Materials https://www.facebook.com/allaboutalgae/photos/a.371644646330812.1073741825.371642179664392/371645722997371/?typ e=3&theater
  • 22.
  • 23.
  • 24. Analysis of Information Length: 15.19 m Width: 28.35 m Depth: 0.61 m SA: 375.37 m2 V: 228.825 m3 or 228,824.6 L *See appendix for calculations
  • 25. Synthesis of Design - Advantages and Disadvantages of Culture Depth Culture depth: 0.25 to 0.34 m Advantages: โ— Biomass concentration is higher Disadvantages: โ— Greater temperature fluctuation โ—‹ Water Temperature Fluctuations (Morning -> Mid afternoon, May - September) โ–  ฮ”T = 12.6 ยฐF (for d = 0.30 m) โ–  ฮ”T = 5.4 ยฐF (for d = 0.61 m) Culture depth: 0.34 m to 0.61 m Advantages: โ— Easier and less expensive to mix Design culture depth = 0.61 m
  • 26. Water Volume Calculations Assuming water evaporates from the surface1 at 0.5 cm/day: Water loss due to evaporation: 1.88 m3/day or 1876.84 L/day Assuming Clemsonโ€™s average annual precipitation2: 127.36 cm/yr: Water gain due to rainfall: 1.31 m3/day or 1309.73 L/day Change in water per day: ฮ” = -567.11 L/day = -0.567 m3/day
  • 27. Water Quality Results Samples from Hunnicutt Creek, Seneca River, and a well near the plot of land were tested. Desired water quality parameters were met for all 3 sources. Therefore, we decided to use economics and logistics as our main criteria for choosing water source. Image from Google Maps
  • 28. Cost Analysis of Water Sources Seneca River: $6,640.00 โ— Includes pipe installation for 280.0 m and 2 HP pump Hunnicutt Creek: $11,320.00 โ— Includes pipe installation for 516.1 m and 2 HP pump Well water: $7,015.00 โ— Less variability in water quality, and less disturbance of surrounding area Municipal water: $1,200.00 โ— Includes pipe installation for 57.6 m
  • 29. Drilling a Well Total Price: $7,015.00 Item Description Price 6โ€™โ€™ drilled well: 30โ€™ @ $12/ft $3600.00 6โ€™โ€™ PVC casing: 70โ€™ @ $5/ft $350.00 Bentonite Grout $150.00 Well Seal $25.00 Permit $70.00 ยพ HP 10gal/min Schaefer Submersible Pump $1,100.00 260 ft 1โ€™โ€™ Schedule 80 Pipe and 12/3 Pump Wire in Well $520.00 PC144 44 gal tank, pressure switch, gauge, and misc. fittings $700 Ditch, Pipe, and Wire to system $350 Breaker and wire from tank to electrical panel $50 Small Rock Cover $100
  • 30. Algae & Inoculation โ— Chlorella vulgaris โ— Common green algae โ— Matches or is close to algae used in reference literature โ— Valuable bioproducts Chlorella vulgaris https://botany.natur.cuni.cz/algo/database/node/110
  • 31. Algae & Inoculation Steps to inoculate PAS units: 1. Receive flask stock culture 2. Transfer to 500-1000 mL beakers a. with Boldโ€™s Basal medium 3. Transfer to 19 L bottles a. At least 0.5 g/L cell concentration 4. Three 19 L bottles per unit a. Allow 4 - 6 weeks for peak biomass
  • 32. Flow Diagram Sketch by Emily Mass Balance Schematic of CSTR with Internal Cell Recycle
  • 33. Mass Balance Approach for CSTR w/ Recycle โ— Utilizing mass balances and Monod kinetics โ—‹ Determine whether system needs external inorganic carbon inputs to achieve goal of 10 g C/m2/day Mass balance and Monod kinetic equations used in Excel
  • 34. Mass Balance Approach for CSTR w/ Recycle โ— No addition of external inorganic carbon needed for system Cell Retention Time (ฮ˜) (hr) 48 Hydraulic Retention Time (ฯ„) (hr-1) 14.75 Specific Growth Rate (ฮผ) (hr-1) 0.023 Rate of Biomass Formation (rXB) (g/m2/day) 27.99 Rate of Carbon Productivity (rS) (g/m2/day) 10.03
  • 35. Nutrient Addition Nutrient g/unit/week g/system/week Nitrogen 518.00 2072.00 Phosphorus 160.00 640.00
  • 36. Synthesis of Design: Degree of Mixing Mixing in an open raceway may increase algal productivity by: โ— Increasing the exposure of the algal cells to sunlight โ— Enhance vertical mixing โ— Preventing cell settling โ— Prevent thermal stratification 2 options assessed to achieve design flow of 0.125 m/s: (1) air lift pump; (2) paddlewheel
  • 37. Air Lift Pump Source: Effortless Aquaponics pressure โ— Estimated cost: $2,900.00 โ— Testing and research needed to determine if desired flow for operating conditions can be achieved.
  • 38. Paddlewheels Paddlewheels are the traditional and most commonly used method of flow and mixing Uniform water velocities can easily be achieved with the use of low rpm (1- to 3-rpm) paddlewheels Pentair Paddlewheel Assembly (PW11-AQ) Cost per unit: $1,112.00 Total cost for system: $4,448.00
  • 39. Algae Separation โ— 1 x 3.5 m belt โ— Duck cloth or canvas belt โ— 4 rpm or 3.8 cm/s โ— Harvest every 7 days โ— Frame 1.1 x 1.2 x 1.5 m Source: Iowa State University
  • 40. Algae Separation Cost Analysis โ— Motor - $300.00 each โ— Rollers - $345.00 per roller, $1,035.00 per unit โ— Belt - $100.00 each โ— Frame - $210.00 steel angle iron โ— Other - $150.00 paint, feet, and fittings โ— Total - $1795.00 per unit, $7,180.00 total
  • 42. Instrumentation Campbell Scientific AquaOne plus AquaBuoy System โ— Performs automated monitoring, control, and alarm functions in recirculating, flow-through, and open-pond aquaculture. โ— Designed to measure input from water-quality, flow, and amp sensors, and control aerators, pumps, alarms, and communication devices. โ— Almost any sensor can be used, including dissolved oxygen, temperature, pH, conductivity, salinity, turbidity, ORP, ammonia, flow, and level Price: $1,495.00
  • 43. Fencing Simple fence estimated at: โ— 4 ft. T - post, 71 units: $260.00 โ— Welded wire, 4 x 100 ft., 4 rolls: $280.00 โ— Amethyst Falls Wisteria, 17 plants: $255.00 โ— Blackberry bush, 28 plants: $205.00 โ— Total: $1,000.00 โ— Total w/ 10% labor: $1,100.00 Amethyst Falls Wisteria Source: www.theplantingtree.com
  • 44. Ground Cover Ground cover to solve problem of mowing: 1 ft of gravel estimated at: โ— Recycled 57 stone: ($16/ton)(1.21 ton/yd3)(128.718 yd3)(โ…”) = $1661.32 โ— Recycled crusher run: ($10/ton)(2 ton/yd3)(128.718 yd3)(โ…“) = $858.12 โ— Total: $2519.43 โ— Total w/ 20% labor & delivery: $3023.00
  • 45. Sustainability Measures โ— Recycling water from PAS โ— Carbon capture by algae โ— Potential for creation of sustainable materials โ— Educational aspect
  • 46. Budget: Total cost of implementation: $144,186.23 Concrete: $101,470.43 Paddlewheel: $4,448.00 Well Installation: $7,015.00 Algae Capture System: $7,180.00 Instrumentation: $1,495.00 Ground Cover: $3,023.00 Fencing: $1,100.00
  • 47. Budget - Operating Costs Description Energy Usage (kW-hr/day) Paddlewheel 17.88 Inflow Pumps (2 EA) 1.024 Algae Collectors 14.32 Total Energy Usage 33.22 Solar array required: 10kW system Total System Cost: $18,454.80 Area Requirement: 600 ft2
  • 48. Conclusions: Water Source: โ— Well water to operate PAS Algae Capture: โ— Mechanical belt system Nutrient Addition: โ— No external inorganic carbon needed to achieve goal โ— Add 2072.00 g N/week and 640.00 g P/week PAS Elevation: โ— 2 ft deep โ— 2 ft above ground Mechanical Flow Device: โ— Paddlewheel to achieve 0.125 m/s flow velocity
  • 49. 3 Questions of the User: BE faculty/students 1. How often does algae need to be harvested? โ— Approximately every 7 days 1. How often/how much nutrient needs to be added to the system? โ— Weekly addition of 2072 g Nitrogen and 640 g Phosphorous 1. What maintenance will be required? โ— Weekly maintenance is required to remove the algae, the water parameters are all monitored by sensors continuously. PAS will need to be maintained at the beginning of each May (growing season) 1. Can this system be altered to allow for fish cultivation? โ— Yes, by removing the algae capturing device and adding additional fish feed, fish can be added
  • 50. 3 Questions of the Client: Ag. Department 1. What are the upfront costs of installation (piping, pump, concrete, etc)? โ— Total overall cost: $145,690.89 1. What are the operating costs? โ— Dependent on energy source used 1. What future research can come from this system? โ— Adding a greenhouse for seasonal extension โ— Operating the system with fish or other aquatic organisms โ— Testing varying algal capturing mechanisms for max algal yield โ— Determining possibilities of air lift pumps for forced flow
  • 51. 3 Questions of the Design Team: 1. What is the most efficient way to capture the algae? โ— For our system, mechanical belt system 1. What water velocity in the channel will produce the highest yield of algae? โ— During the day: 0.125 m/s 1. What cell retention time would meet our carbon productivity goal? โ— 48 hours
  • 53. References/Patents 1. Brune, D., et al. (2004).19 Partitioned Aquaculture Systems: Biology and Culture of Channel Catfish Developments in Aquaculture and Fisheries Science pp. 561โ€“584., https://doi.org/10.1016/s0167-9309(04)80021-8. 2. Caswell, W.; Norvell, K. (2016) Algal harvesting in the Partitioned Aquaculture System: Clemson University, BE 4750 Senior Design 3. Chisti Y. (2016). Large-Scale Production of Algal Biomass: Raceway Ponds: Algae Biotechnology pp 21-40. https://doi.org/10.1007/978-3-319-12334-9_2 4. Clark, N, Dabolt, R. (1986) A General Design Equation for Air Lift Pumps Operating in Slug Flow: AiChE Journal pp 56-64. doi: 10.1002/aic.690320107 5. Drapcho, C., Brune, D. (2000). The partitioned aquaculture system: Impact of design and environmental parameters on algal productivity and photosynthetic oxygen production: Aquacultural Engineering. 21. 151-168. https://doi.org/10.1016/S0144-8609(99)00028-X
  • 54. References/Patents 6. Gross, M 7. Mandal S, Mallick N. Biodiesel Production by the Green Microalga Scenedesmus obliquus in a Recirculatory Aquaculture System: Applied and Environmental Microbiology. 2012;78(16):5929-5934. doi:10.1128/AEM.00610- 12. 8. Swann, L. A Fish Farmerโ€™s Guide to Understanding Water Quality: Illinois-Indiana Sea Grant Program Purdue University 9. Turker, H., Eversole, A., Brune, D. (2003). Filtration of green algae and Cyanobacteria by Nile tilapia, Oreochromis niloticus, in the Partitioned Aquaculture System: Aquaculture. 215. 93-101. https://doi.org/10.1016/S0044-8486(02)00133-3. 10. Wurts, W, McNeill, S, Overhults, D. (1994). Performance and Design Characteristics of Airlift Pumps for Field Applications: World Aquaculture: 25(4): 51-55. http://www2.ca.uky.edu/wkrec/AirliftPumps.htm
  • 55.
  • 56. Appendices - Volume Calculations
  • 57. Appendices - Structural Calculations
  • 58. Appendices - Water Quality Test (Hunnicutt)
  • 59. Appendices - Water Quality Test (Seneca River)
  • 60. Appendices - Water Quality Test (Well Water)
  • 62. Appendices - Design Calculations
  • 63. Appendices - Air Lift Pump Equations โ— Solving for Velocity: โ—‹ Vg= Vw * [โดwgL/P2ln(P0/P2)] * โ—‹ L = 0.05 m โ—‹ P2 = 101 kPa = 101,000 kg/m*s2 โ—‹ P0 = P2 + โดwgh = 106,000 kg/m*s2 โ—‹ g = 9.81 m/s2 โ—‹ โดw = 1000 kg/m3 โ—‹ Vw = Velocity of effluent water (m/s) โ—‹ Vg = Velocity of injected gas (m/s)
  • 64. Appendices - Air Lift Pump Equations (Cont.) โ— Modified Bernoulliโ€™s equation: โ—‹ แน0(V0 2/2g + h0) + แน1(V1 2/2g + h1) = แน2(V2 2/2g + h2) + ฮ”hf โ—‹ แน = mass flow rate (kg/s) โ—‹ V = velocity (m/s) โ—‹ g = 9.81 m/s2 โ—‹ h = height (m) โ—‹ ฮ”hf = friction loss (m)

Editor's Notes

  1. AB: PAS developed at Clemson in 1989 https://thefishsite.com/articles/partitioned-aquaculture-systems
  2. AB:
  3. AB:
  4. ES:
  5. ES:
  6. ES:
  7. E:
  8. KK Critical design parameters for continuous algal culture systems include cell retention time, nutrient addition rate, water depth, and degree of mixing
  9. KK
  10. KK
  11. KK
  12. A: https://www.was.org/Documents/MeetingPresentations/WA2005/WA2005-541.pdf https://www.slideshare.net/KateyNorvell/algal-harvesting-in-the-partitioned-aquaculture-system
  13. A: โ€˜To start out with, we want to go over heuristics our group came into this project with. All this experience blah blah blah. This heuristics allowed us to come up with our governing equationsโ€™
  14. A: https://thefishsite.com/articles/partitioned-aquaculture-systems โ€˜Different classes used these equations. We used what we knew in biological kinetics along with these equations to determine the nutrients required to operate the PASโ€ฆ.โ€™
  15. A: โ€˜...And we used these fluids equations to calculate various parameters for the mechanical systems: paddlewheel and airlift pumpโ€™
  16. A:
  17. E: The PAS was designed and patented at Clemson University by Dr. Drapcho and Dr. Brune. Their published research on the PAS was used to obtain many of the design goals for our project. We used the maximum algal productivity rate of 10 g C/m^2/day and their optimimum results for cell retention retention time and water velocity. This research was conducted to establish relationship between algal productivity in the PAS as a function of these different variables.
  18. E:
  19. E: Explain differences between original system and new design
  20. E:
  21. E: Determined we could not use rain barrel as water source
  22. E: The advantage of increased algal productivity must be weighed against the disadvantages of shallow culture depths
  23. K: Based on water needed per day, canโ€™t use rain barrel
  24. K: Redo entire slide. Based on water quality results all water sources are similar. So used cost of implementation as deciding factor
  25. K: Use to initially fill the PAS (90673.599 gal) at $3.36/1000 gal โ†’ Cost: $304.66 Used a value of $120/20 ft for estimated pipe costs (Heuristics via Emilyโ€™s co-op) Used ArcGIS Online to measure lengths Used $3.36/1000 gal for inside Clemson city limits municipal (not irrigation, though thatโ€™s $1.11/1000 gal); can tie into Organic Farm water for minimal start up costs
  26. Jet pump, $300-$500 Wiring and piping, $300-$400
  27. A Rapid growth Often used in photobioreactors Used in vitamins and foods Can be used for biofuels due to high lipid content
  28. A
  29. Design cell retention time is 1-3 days but flow conditions we need are conflicting with the retention time. In order to increase cell retention time we must recycle biomass into system. Qw -- Q waste is not actually waste, this would be used as a byproduct for biofuels or whatever else
  30. Using mass balances for a CSTR with recycle at steady state and Monod kinetics I was able to model our system to determine whether it would require external additions of inorganic carbon to achieve our goal of 10 g C/m2/day
  31. Using a mass balance with respect to inorganic carbon, I manipulated the cell retention time and determined the specific growth rate. Using that specific growth rate I was able to solve for the rate of carbon productivity in the system.
  32. Nitrate NO3- Ammonium nitrate Hydrogen Phosphate
  33. A
  34. A 2 Regenerative air blowers: $1900 $700 6โ€ PVC $30k0 2โ€ PVC & fittings
  35. This paddlewheel assembly is the most commonly available on the market for aquaculture. The motor is insulated by plastic and the floats allow for the assembly to move with varying water depths. The electric motor has the ability to be powered by solar panels which further meets our design criteria of decreasing energy usage.
  36. A: http://www.sciencedirect.com/science/article/pii/S0960852413015964
  37. Angle iron: 1 ยพโ€ x 1 ยพโ€ x ยผโ€ Conveyor support dimensions: 1.5 m tall. 1.1 m wide, 1.2 m long Total of 15.2 m of angle iron 562.88 kW/hr/month * 4 = 2251.52 kW/hr/month
  38. K:
  39. K: AquaOne plus AquaBuoy Bullet slide; talk about CR10X chip
  40. A: Wisteria every 10 ft: 35 plants 35 plants @ $15: $527.1 17 plants @ $15: $255 Blackberries: Every 5 ft: 70.28 71 plants @ $7.33: $500 35 plants @ $7.33: $257
  41. 57 stone is mixed gravel <1โ€ Crusher run is very fine dirt/dust mixed with stones with 1 ยฝโ€ and smaller
  42. K:
  43. K:
  44. Kayla cite: https://www.cityofclemson.org/Portals/0/CoCDepartments/Finance%20and%20Utility%20Billing/Billing%20Administration/2016%20RATE%20SCHEDULE.pdf
  45. https://www.extension.purdue.edu/extmedia/as/as-503.html https://www.ncbi.nlm.nih.gov/pmc/articles/PMC3406171/