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![Page 1: UT OpenAlgae Oil Recovery Frank Seibert UT/Separations Research Program Presented to CHE 359 Energy Technology and Policy November 17, 2011.](https://reader030.fdocuments.us/reader030/viewer/2022032723/56649d175503460f949ed5f0/html5/thumbnails/1.jpg)
UT OpenAlgae Oil RecoveryUT OpenAlgae Oil Recovery
Frank SeibertUT/Separations Research ProgramPresented to CHE 359 Energy Technology and Policy November 17, 2011
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Process TechnologiesProcess Technologies
Heterotrophic Algae Solution
Ferment recover oil & biomasslyse
Photosynthetic Algae Solution
Grow recover oil & biomass
harvest/ concentrat
elyse
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OpenAlgae andThe University of Texas Algae Program
grow algae 4-stage scale-up to raceway ponds
strain selection -- over 3,000 strains readily available through UTEX
species-customized to maximize lipid or protein content
daily analyses of lipid and protein content
harvest/ concentrate
multiple concentration methods under exploration
pH adjustment proprietary resin technology
proprietary electrowicking process
test and measure
• identify and quantify the types of lipids present in algae• follow the abundance of lipids in algae through growth, harvest, lysis and extraction• determine the composition of the final oil
MassSpecHPLC NMRTLC
mobile platform
Mobile & skid-mounted trans-portable units
pilot or production scale unit will harvest, lyse, and extract oils from algae
biomass remains untainted by solvents and can be sold for downstream applications
lyse patented technology opens cells and exposes lipid droplets via electromechanical forces
solvent-less system maintains the integrity of the algal biomass
works on fresh, brackish, and marine algae
extremely cost efficient
UT OpenAlgae Technologies
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Challenges• Micron-size algae • Very small density difference• Negatively charged• Dilute concentrations• High volumes
Considerations • Algae species (mix)• Water composition
- Brackish/fresh- Conductivity, pH, ionic composition
• Paste or pumpable product• Byproducts
multiple concentration methods under exploration
pH adjustment proprietary resin technology
proprietary electrowicking process
harvest/ concentrate
Algae harvestingAlgae harvesting
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Electromechanical lysingElectromechanical lysing
Lysis is a continuous process for wet algae and is species–neutral – lysis opens the cells and exposes lipid droplets via electromechanical forces
lyse patented technology opens cells and exposes lipid droplets via electromechanical forces
solvent-less system maintains the integrity of the algal biomass
works on fresh, brackish, and marine algae
extremely cost efficient
Post-Lysis
Prior to Lysis
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Lysing capabilities
Tunable, custom pulsing to rupture cells
Works with mono- and poly-cultures
Continuous flow, scalable throughput
Operating cost <$0.01 per gallon of concentrated cells lysed
Power use varies with conductivity of media
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Algae Oil RecoveryAlgae Oil Recovery
• Process Options• The Problem• New Algae Oil Recovery Technique
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Oil Recovery FocusOil Recovery Focus
• Cost Effective Liquid Fuel (Priority) - Recovery of non-polar hydrocarbon - No Phospholipids• Simple Process• No Contamination of Biomass Effluent
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LipidsTEM provided by Colin Beal, Dr. Dwight Romanovicz and Christopher Mayer
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“Dry Process” “Dry Process”
Separate Waterand Algae
Feed:ConcentratedAlgae Slurry
Water
Algae Paste orPowder
Solvent
Lysing andOil Recovery
Separate algaeand solvent(and water)
Separate oiland solvent
Lysing and Oil Recovery
Separate oiland solvent
Separate waterand algae
Solvent
“Wet Process”
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Lysing and Extraction
Oil
Separate waterand algae
“Solventless Process”
ConcentratedAlgae Slurry
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Oil Recovery ProblemOil Recovery Problem• Efficient cell destruction required• Submicron nonpolar lipid drops• Surface active chemicals released• Presence of cell debris• Large fraction of algae oil is non-polar and may not be
desirable for fuel - Phospholipids will poison downstream catalyst• Preservation of biomass for animal feed
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Dispersive Contactor TechnologiesDispersive Contactor Technologies
• Centrifuge• Trayed • Enhanced Trayed
• All dispersive techniques using solvents Problems with emulsions
Liquid-Liquid Extraction
Lysed AlgaeConcentrate
Solvent
Extract
Raffinate
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14
MHF Membrane ContactorMHF Membrane Contactor
Lysed Algae FeedWith Oil
Oil
Algae Raffinate
Oil
Microporous Hollow-Fiber Membrane
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Hollow Fiber DimensionsHollow Fiber Dimensions
16
Dimensions in mm0.1 mm = 100 microns
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Microporous Hollow Fiber ContactorMicroporous Hollow Fiber Contactor• Provisional process patent application filed
US61/295,607• Non-provisional patent filed in January 2011• Supported with pilot data• Proposed mechanism – coalescence• No signs of fouling/One module in operation for
12 months• Size of hydrophillic micro-organism < 30 microns
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Typical MHF Extractor Performance with Actual Algae Oil Extraction Using Heptane
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Solventless Test-Initial ResultsSolventless Test-Initial Results
Tube side = canola oilShell side = 2 wt% solids previously lysed and extracted algaeRe-circulating flowsTube-side flow = 10-15 lbs/hrShell-side flow = 500 lbs/hrOil injection rate into shell-side slurry = 3 ml/min (4% oil in solids)Run time = 72 hours (4-5 shutdowns to monitor oil accumulation)
Recovery of injected canola oil = 93%
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Membrane SkidMembrane Skid
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Current Solventless Tests
Tube side = Isopar VShell side = water with and without algae solidsRe-circulating flowsTube side flow = 0-10 lbs/hrShell-side flow = 500 lbs/hrOil injection rate into slurry = 1.5 - 3 ml/min (~5% oil in solids)Run time = 120 - 168 hours (daily shutdown to monitor oil
accumulation)
Steady State Oil Recoveries > 94%
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Oil Concentration in Water = 0.5 g oil/L (No Solids) Large Module
Oil Recovery Using Solventless Process
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Oil Recovery from WaterWater Flowrate (large module) = 500 lb/hrWater Flowrate (small module) = 250 lb/hr
Oil Recirculation Rate = 0
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Oil Recovery in the Presence of Algae Solids Oil Concentration in Water = 0.5 g oil/L (1% Solids) Large Module
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Portable 5 GPM Algae Processing System
Algae ConcentrationLysing
Oil Recovery
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OpenAlgae Mobile Algae Processing
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Lysing chamber &
power supply
Concentrationskid
Oil Recoveryskid
OpenAlgae Mobile Algae ProcessingOpenAlgae Mobile Algae Processing
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Energy Return on Investment for Algal Biofuel
Energy Return on Investment for Algal Biofuel
Biofuel Production
Biofuel Production
inE outE
Colin Beal, PhD Dissertation, The University of Texas at Austin, 2011
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The Energy Return on Investment is a useful metric to evaluate energy sources
The Energy Return on Investment is a useful metric to evaluate energy sources
EROI:1)Crude Oil (2000) – 202)Coal (2000) – 803)Wind Energy (2009) – 204)Sugar Cane Ethanol (2005) – 95)Corn Ethanol (2007) – 16)Algal Biofuels - ?
Cleveland C.J., 2005.Kubiszewski et al., 2009Macedo et al., 2008
Energy SystemEnergy System
Energy and Material
Inputs
Energy Output
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Algal Culture
Harvested Algae
Useful Energy Outputs
Direct and Indirect Energy Inputs (Beal PhD Study)
Lysed Algae
Post-Extraction Algae and Lipids
Water CO2
ElectricityNutrients
Electricity
Solvent
Algae Inoculants
BiocrudeBiomass Slurry
Electricity
Electricity
System Boundary
Salt
Antibiotics
Forklift Propane
Bio-oil
Refining Inputs
Biomass Fuel
From Beal et al., “Energy Return on Investment…”, BioEnergy Research, In Review.
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Energy Return on Investment“Highly Productive Case”
Energy Return on Investment“Highly Productive Case”
Process % of Energy
Required,
Growth 89% (CO2) (79%)
Concentration 10.5%
Lysing 0.25%
Separations (with Dist) 0.25%
Total Energy ~ 75 KJ/L pond water
Algae Growth Rate = 16 g/m2-dayLipid Fraction = 0.3 g/gEnergy Recovered = 16.6 KJ/L
EROI = 16.6/75 = 0.22
Reference: Beal, C., PhD Dissertation, The University of Texas at Austin, 2011
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1) Use waste forms of nitrogen and phosphorus or recover for
recycle2) Use flue-gas from industrial plants or atmospheric CO2
3) Develop ultra-productive algal strains (GMO)4) Minimize pumping5) Establish energy-efficient water treatment and recycling6) Employ less energy-intensive harvesting methods
Needs to Improve the Feasibility of Algal Biofuels:Needs to Improve the Feasibility of Algal Biofuels:
Reference: Beal, PhD Dissertation, The University of Texas at Austin, 2011.
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SummarySummary• UT OpenAlgae has developed downstream solventless oil
recovery process• Greater than 90% oil recovery in controlled oil injection
studies• Need field testing• Requires efficient lysing for microorganisms that do not
secrete oil• Not effective for flocculated microorganisms• Recovery mechanism – coalescence • Algae processing is limited in the growth step
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AcknowledgementsAcknowledgements
•OpenAlgae•Separations Research Program•Katie O’Brien•Stacy Truscott