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PRODUCTION OF ALGAL OIL
BE 4380
Kira Bartlett & Cassidy Laird
INTRODUCTION
• Algae as Feedstock
– Normally food supplements
• Need better Energy Resources
– Algal conversion of solar energy
• Harvestable Form
• More efficient
• Carbon Neutral Process
PROCESS DESIGN
Annual Biomass Production: 275,000 MT
Annual Algal Oil Production: 65,000 MT
SONICATOR
• High Pressure Homogenization
• Disrupts algae cells to release the lipids
100 Biomass  7 ASH + 42.2 Cell Debris + 0.8 NHP + 4 PL + 4 Proteins + 26 TAG
CENTRIFUGATION
Component separation based on density
Centrifugal/Centripetal force in radial direction
DECANTER CENTRIFUGE
DISK STACK CENTRIFUGE
• Separates TAG and other lipids from stream
• Alter rotational velocity, efficiency, etc.
• Balance with cost and power
HEXANE EXTRACTION
• Extracts remnants of lipids
• Balanced stoichiometric equations
– Difficult to alter process
ECONOMIC EVALUATION
• Startup Costs: $305,344,000
YEARLY EVALUATION
• Operating Cost: 98,723,849
– Initial Operating Cost: $111,793,000
– Savings: $13,069,377
• Revenues: $126,603,051
• Profits: $13,069,378
Break Even Point: 6.94 yrs
ALTERNATIVES CONSIDERED
• Type of Algae
• Methods of lipid extraction
• Parameters on disk-stack centrifuge
CONCLUSIONS
• Working facility to produce Algal Oil
– Used for generation of clean energy
• Creates other Valuable Products
– Proteins for Animal Feed
– Electrical Energy Produced
• Reduces & Reuses Waste Products
– Organic & Aqueous Wastes
– Low Emissions
– Less Bulk Materials needed
REFERENCES
Alfa Laval. Inflatable dam for a decanter centrifuge. US Application No. 92 904 608.2
Alfa Laval Corporate AB. Disk stack separator technology. PDF.
Ashokkumar, V., Z. Salam, P. Sathishkumar, T. Hadibarata, A. Yusoff, F. Ani. Exploration of fast growing Botryococcus sudeticus for
upstream and downstream process in sustainable biofuels production. Journal of Cleaner Production 92(1): 162-167.
Demirbas, A., M.F. Demirbas. Importance of algae oil as a source of biodiesel. Energy Conservation and Management 52(1): 163-170.
Kiran, B., R. Kumar, D. Deshmukh. Perspectives of microalgal biofuels as a renewable source of energy. Energy Conservation and
Management 88: 1228-1244.
Intelligen, Inc. Algal Oil Production: Modeling and Evaluation Using SuperPro Designer. Intelligen: 1-26.
Samarasinghe, N., S. Fernando, R. Lacey, W.B. Faulkner. Algal cell rupture using high pressure homogenization as a prelude to oil
extraction. Renewable Energy (48): 300-308.
Sheehan, J., T. Dunahay, J. Benemann, P. Roessler. A Look Back at the U.S. Department of Energy’s Aquatic Species Program – Biodiesel
from Algae. National Renewable Energy Laboratory: 2-8.
Shenglei, B., D. Fengguang, S. Peiyong, et al. 2014. Oil extraction method of heterotrophic chlorella. Application No. CN2014194147
20140314
Sudhakar, K., M. Premalatha, K. Sudharshan. 2012. Energy Balance and Exergy Analysis of large scale algal biomass production. The 2nd
Korea-Indonesia Workshop & International Symposium of Bioenergy from Biomass: 66-69.

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Algal oil kira & cassidy

  • 1. PRODUCTION OF ALGAL OIL BE 4380 Kira Bartlett & Cassidy Laird
  • 2. INTRODUCTION • Algae as Feedstock – Normally food supplements • Need better Energy Resources – Algal conversion of solar energy • Harvestable Form • More efficient • Carbon Neutral Process
  • 3. PROCESS DESIGN Annual Biomass Production: 275,000 MT Annual Algal Oil Production: 65,000 MT
  • 4. SONICATOR • High Pressure Homogenization • Disrupts algae cells to release the lipids 100 Biomass  7 ASH + 42.2 Cell Debris + 0.8 NHP + 4 PL + 4 Proteins + 26 TAG
  • 5. CENTRIFUGATION Component separation based on density Centrifugal/Centripetal force in radial direction
  • 7. DISK STACK CENTRIFUGE • Separates TAG and other lipids from stream • Alter rotational velocity, efficiency, etc. • Balance with cost and power
  • 8. HEXANE EXTRACTION • Extracts remnants of lipids • Balanced stoichiometric equations – Difficult to alter process
  • 9. ECONOMIC EVALUATION • Startup Costs: $305,344,000 YEARLY EVALUATION • Operating Cost: 98,723,849 – Initial Operating Cost: $111,793,000 – Savings: $13,069,377 • Revenues: $126,603,051 • Profits: $13,069,378 Break Even Point: 6.94 yrs
  • 10. ALTERNATIVES CONSIDERED • Type of Algae • Methods of lipid extraction • Parameters on disk-stack centrifuge
  • 11. CONCLUSIONS • Working facility to produce Algal Oil – Used for generation of clean energy • Creates other Valuable Products – Proteins for Animal Feed – Electrical Energy Produced • Reduces & Reuses Waste Products – Organic & Aqueous Wastes – Low Emissions – Less Bulk Materials needed
  • 12. REFERENCES Alfa Laval. Inflatable dam for a decanter centrifuge. US Application No. 92 904 608.2 Alfa Laval Corporate AB. Disk stack separator technology. PDF. Ashokkumar, V., Z. Salam, P. Sathishkumar, T. Hadibarata, A. Yusoff, F. Ani. Exploration of fast growing Botryococcus sudeticus for upstream and downstream process in sustainable biofuels production. Journal of Cleaner Production 92(1): 162-167. Demirbas, A., M.F. Demirbas. Importance of algae oil as a source of biodiesel. Energy Conservation and Management 52(1): 163-170. Kiran, B., R. Kumar, D. Deshmukh. Perspectives of microalgal biofuels as a renewable source of energy. Energy Conservation and Management 88: 1228-1244. Intelligen, Inc. Algal Oil Production: Modeling and Evaluation Using SuperPro Designer. Intelligen: 1-26. Samarasinghe, N., S. Fernando, R. Lacey, W.B. Faulkner. Algal cell rupture using high pressure homogenization as a prelude to oil extraction. Renewable Energy (48): 300-308. Sheehan, J., T. Dunahay, J. Benemann, P. Roessler. A Look Back at the U.S. Department of Energy’s Aquatic Species Program – Biodiesel from Algae. National Renewable Energy Laboratory: 2-8. Shenglei, B., D. Fengguang, S. Peiyong, et al. 2014. Oil extraction method of heterotrophic chlorella. Application No. CN2014194147 20140314 Sudhakar, K., M. Premalatha, K. Sudharshan. 2012. Energy Balance and Exergy Analysis of large scale algal biomass production. The 2nd Korea-Indonesia Workshop & International Symposium of Bioenergy from Biomass: 66-69.

Editor's Notes

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