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University of Kentucky CAER-Duke Energy East Bend Algae Demonstration Project
Dr. Jack GroppoUniversity of Kentucky
Center for Applied Energy Research
Lexington, KY
National Coal Council2015 Annual Fall Meeting
November 4-5, 2015
Project Timeline
• 2008 – UK Approached by Kentucky Department of Energy Development and Independence to investigate the techno-economic feasibility of algae based CO2 mitigation
• 2011-2012: Initial Demonstration Work started at EKPC’s Dale Station
• 2012-Present: Demonstration Project at Duke Energy’s East Bend Station
• 2011-Present: Part of US-China Clean Energy Research Center (CERC)
• August, 2015: NETL Biological CO2 Utilization Award
• Research Focus Areas– Power Plant Integration
– PBR Design/Operation
– Dewatering
– Techno-economic modeling
– Utilization
• Utilization Focus Areas– Bio-polymers
– Lipid Extraction
– Catalytic Upgrading
– HTL
– Pyrolysis
– Aquaculture
– Anaerobic Digestion
Catalytic Upgrading of Lipids
Gravity Filtration
Fuel Like Hydrocarbons
CO2 as flue gas Cultivation in low cost PBR Flocculation/Sedimentation
M.H. Wilson, J. Groppo, E. Santillan-Jimenez, M. Crocker et al., Appl. Petrochem. Res. 4 (2014) 41
Overall Concept: CO2 Utilization
Bio-Plastics
Current Research Focus
5
Solar modeling for optimum photobioreactor spacing
Continuous Dewatering
Flow Chart of Process With Research Focus Areas Highlighted in Blue
• Pilot algae facility at Duke Energy’s East Bend Station in 2012
1st generation UK photobioreactor (top)
• Primary PBR Components3.5” d x 8’ tall clear PET packaging tubesPVC pipe fittings
• Routine Areal productivity≥ 0.25 g/l/day (summer) ≥ 0.10 g/l/day (winter)
• System Volume18,000 L/5,000 gallons
• New “cyclic flow” photobioreactordeployed in 2014 (bottom)
lower costhigher productivitymore robust operation
Field Demonstration
Field Demonstration
Cyclic operation to• reduce energy costs• control biofilm formation
Harvesting/Dewatering Flowsheet
8
PRIMARYTHICKENER
HORIZONTAL FILTER/SOLAR DRYER
240 gallons
2' x 8'
0.4 g/l0.04% solids
20 to 30 g/l2% to 3% solids
175 g/l7.5% to 25%
solids
UV STERILIZER
Recycle toFeed Tank
<0.01 g/l<0.001 % solids
9
During
• Multifilament nylon media for rapid cake formation and high solids capture (>99%)
• Allows separation and recycling of all free water containing unused nutrients
• Short vacuum pulse after cake formation can improve throughput
• Can produce 10-25% solids for utilization• Solar oven can reach 60oC in summer
Prototype Gravity Filter/Solar Dryer
97.9%
1.5%
0.6%
Distribution of Water in Harvest Cycle
ThickenerOverflow
FilterFiltrate
Filter Cake
Harvest/Dewatering: Typical Results
10
30
0.45 0.170.4
25.3
72.5
0
10
20
30
40
50
60
70
80
Thickener Feed Filter Feed Filter Cake
Volume, liters
Culture Density, g/l
System Productivity
0
2
4
6
8
10
12
14
16
18
20
0
5
10
15
20
25
30
35
40
45
50
55
605
-May
8-M
ay
11-
May
14-
May
17-
May
20-
May
23-
May
26-
May
29-
May
1-J
un
4-J
un
7-J
un
10-
Jun
13-
Jun
16-
Jun
19-
Jun
22-
Jun
25-
Jun
28-
Jun
1-J
ul
4-J
ul
7-J
ul
10-
Jul
13-
Jul
16-
Jul
19-
Jul
22-
Jul
25-
Jul
28-
Jul
31-
Jul
3-A
ug
6-A
ug
9-A
ug
12-
Au
g
15-
Au
g
18-
Au
g
21-
Au
g
24-
Au
g
27-
Au
g
30-
Au
g
Tota
l PA
R, µ
mo
l/m
2/d
ay x
E9
Aer
ial P
rod
uct
ivit
y, g
/m2
/day
East Bend TBO May 5 - Aug 30
Flue Gas Bottled CO2 PAR
OutageOutage←← →→
Mass Balance Determination
Reactor MeasurementsTemp, dissolved O2, pH
Flue Gas Measurementsinlet and outlet streamsMRU Flue Gas analyzers
Temp, CO2, O2,NOx, SOx, CO, and CH4.
Data measured every 30 seconds and stored automatically.
Mass Balance Data
Indicates CO2
conversion to O2
via photosynthesis.
Highlights opportunity to optimize CO2
conversion. Targeting 75%
Inlet %
CO2 reduction
O2 production
Mass Balance Data: CO2
CO2 Inlet
CO2 Outlet
Temperature
PAR
Mass Balance Data: SOx
-2500
-2000
-1500
-1000
-500
0
500
1000
1500
2000
2500
0
10
20
30
40
50
60
70
9/14/2015 0:00 9/16/2015 0:00 9/18/2015 0:00 9/20/2015 0:00
PA
R (
μm
ol/
m^2
s)
SOx
pp
m a
nd
Tem
per
atu
re (
⁰C)
5 Second Sparge
Tr SOX IN SOX OUT PAR
Algal Biomass Utilization
16
Algal Biomass Utilization Pathways
Current UK Concept for CO2 Capture/Bio-product Production
18
Proposed Layout of a 3 Acre Photobioreactor
Zhengzhou, China
57,600 tubes265,000 gallons
How Big?1 MW 500 MW
Emissions tons CO2/MW 1 1
Emission rate tons CO2/day 24 12,000
@40% CO2 Capture
tons CO2/day 9.6 4,800
@1.78 tons CO2/ton algae
tons algae/day 5.4 2,697
@35 g/m2/day productivity
g algae/day 139,916 69.96x106
Land Required acres 35 17,287
Why Bother?
• CO2 utilization can be revenue positive– Bioplastics
– Biofuels
• While achieving 40% CO2 capture is unreasonable – Marginal CO2 reductions can be achieved profitably
• Offset reduction requirements
Ongoing Collaborations
Cyanidium merolaeDr. Pete LammersAZ State University
Dr. Jennifer Stewart,University of Delaware
Extremophiles
Culture Adaptation
Bioplastics
• Student Employment / Experiential Learning• Undergraduate Engineers, Scientists, and
Architects contribute to day to day research activities
• Senior Design Projects• CAER researchers act as customer/advisor to provide real world projects for student
teams in Mechanical, Electrical, and Chemical Engineering
• Students get exposed to research and researchers at CAER get prototype equipment and/or models to aid research
• College of Design Studios• Architecture and/or Interior Design students work on developing forward thinking
designs, large scale instillations, next generation research facilities, and creative applications of current research
• Graduate Students / Postdocs
Student involvement is an important focus of the project, leveraging creative problem solving and enthusiasm to solve real world research problems while developing the scientists and engineers of tomorrow.
Student Engagement
KY Department of Energy Development and Independence
Duke Energy
Department of Energy: U.S.-China Clean Energy Research Center
The UK algae team:
Dr. Mark CrockerDr. Czarena Crofcheck Tonya Morgan Thomas Grubbs Robert PaceStephanie Kesner Dr. Eduardo Santillan-Jimenez Daniel Mohler Aubrey Shea
and….. ca. 30 students
Acknowledgments
Future Work• Reduce Cost / Increase Productivity
• Optimized photobioreactor design and operation• Batch continuous dewatering process
• Conceptual Design of System Integrated with Power Plant• Mass and Energy Balances
• Power plant integration (heat, flue gas, etc.)
• Life Cycle Assessment
• Techno Economic Analysis
• Biomass Utilization / Valorization• Focus on fuels/chemicals and biopoloymers• Investigate alternative / multi-product utilization pathways• Fate of NOx, SOx, heavy metals
• Systems Biology• Power plant outage mitigation system• Flue gas constituents on biomass composition• Abiotic Parameter Optimization