Bio-Oil from Phototrophic Microorganisms: Innovative Technologies and Strategies
Abstract
1. Introduction
2. Phototrophic Microorganisms as Advanced Feedstocks for Bio-Oil Production
2.1. High Biomass Productivity and Growth Performance
2.2. Lipid Accumulation and Biochemical Composition
2.3. Resource Efficiency and Wastewater-Based Cultivation
2.4. Carbon Fixation and CO2 Utilization
2.5. Compatibility with Integrated Biorefinery Systems
3. Conversion Pathways for Bio-Oil Production from Phototrophic Microorganisms
3.1. Hydrothermal Liquefaction (HTL)
3.2. Pyrolysis
3.3. Catalytic Hydroprocessing (HDO)
3.4. Biotechnological Approaches and Genetic Engineering
3.4.1. Genetic and Metabolic Engineering of Phototrophic Microorganisms
3.4.2. Co-Cultivation and Biological Conversion Pathways
3.4.3. Pretreatment and Extraction Intensification
3.4.4. Wet Biomass Processing and Fuel Stabilization Strategies
4. Integration of Wastewater Streams into Algal Biofuel Production Systems
5. Synthetic Biology Strategies for Enhanced Biofuel Yields
5.1. Systems-Based Metabolic Design
5.2. Process Optimization and Bio-Oil Upgrading
5.3. Integration of Synthetic Biology and Process Engineering
5.4. Future Perspectives
6. Algal Biofuels Within the Circular Bioeconomy Framework
7. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
Abbreviations
| CBP | Consolidated Bioprocessing |
| CCM | Carbon-Concentrating Mechanism |
| CCGT | Combined Cycle Gas Turbine |
| CCU | Carbon Capture and Utilization |
| CO2 | Carbon Dioxide |
| CRISPR | Clustered Regularly Interspaced Short Palindromic Repeats |
| DGAT | Diacylglycerol Acyltransferase |
| DME | Dimethyl Ether |
| DOE | U.S. Department of Energy |
| FAME | Fatty Acid Methyl Esters |
| FDA | Food and Drug Administration |
| GDP | Gross Domestic Product |
| GHG | Greenhouse Gas |
| HHV | Higher Heating Value |
| HTL | Hydrothermal Liquefaction |
| IPCC | Intergovernmental Panel on Climate Change |
| ME | Metabolic Engineering |
| ME-Model | Integrated Model of Metabolism and Macromolecular Expression |
| MSP | Minimum Selling Price |
| PBR | Photobioreactor |
| RSM | Response Surface Methodology |
| SAR | Structure–Activity Relationship |
| SCF | Supercritical Fluid |
| SDGs | Sustainable Development Goals |
| SHF | Separate Hydrolysis and Fermentation |
| SOx | Sulfur Oxides |
| TAG | Triacylglycerol |
| TEA | Techno-Economic Analysis |
| TO | Thermodynamic Optimization |
| VFA | Volatile Fatty Acids |
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| Method | Operating Conditions | Feedstock Type | Main Advantages | Limitations | Bio-Oil Yield and Quality | References |
|---|---|---|---|---|---|---|
| Hydrothermal Liquefaction (HTL) | 300–400 °C; 180–300 bar; aqueous medium | Wet microalgae and cyanobacteria (70–90% moisture) | Direct use of wet biomass (no drying); high energy density (up to 46 MJ/kg); short reaction time | High pressure requirement; product upgrading needed due to N- and O-containing compounds | 45–60% yield; Energy dense, viscous oil with moderate oxygen content | [57,58] |
| Fast Pyrolysis | 450–600 °C; oxygen-free; 100–1000 °C/s heating rate | Dry or lipid-rich algal biomass | Simple process; high oil yield (50–60%); scalable reactors (fluidized-bed) | Requires dry biomass; high O2 and H2O content; oil instability | 50–62% yield (dry basis); oxygen-rich bio-oil requiring upgrading | [59,60] |
| Catalytic Pyrolysis | 450–550 °C with catalysts (HZSM-5, ZrO2, Al2O3) | Lipid-rich algal biomass | Produces aromatics (BTX compounds); improved stability | Reduced overall yield; catalyst deactivation over time | 36–40% aromatics; reduced oxygen and nitrogen content | [61,62] |
| Catalytic Hydroprocessing (HDO) | 200–400 °C; ≥30 bar H2; catalysts (Ni–Mo, Co–Mo, Pt, Pd, Ru) | HTL or pyrolysis bio-oil | Removes oxygen/nitrogen; increases fuel stability; produces drop-in hydrocarbons | High cost of catalysts and hydrogen; complex reactor design | >80% O removal; high calorific value; hydrocarbon fuel-like oil | [63,64] |
| Biotechnological Approaches | Ambient; nutrient/stress-induced lipid accumulation; gene overexpression | Engineered or native microalgae | Increases lipid productivity (up to 2×); enhances CO2 fixation; environmentally friendly | Long development time; scale-up challenges | Lipid content up to 60–70% dry weight; improved fatty acid composition | [65,66] |
| Process Strategy | System | Underlying Mechanism | Outcome | References |
|---|---|---|---|---|
| SAMS overexpression | Chlamydomonas reinhardtii | Enhanced growth and lipid accumulation | 1.5–2× lipid increase | [77] |
| HSbZIP1 transcription factor | Chlorella sp. HS2 | Increased fatty acid content | ~2× fatty acids | [78] |
| ACCase/DGAT overexpression | Engineered microalgae | Redirected carbon flux to lipids | +142% lipid accumulation | [79] |
| Co-cultivation | C. reinhardtii + A. chroococcum | Improved lipid productivity | 19× increase | [80] |
| Cavitation pretreatment | Microalgae biomass | Enhanced lipid extraction | Reduced solvent and energy demand | [81,82] |
| Supercritical alcohol blending | Algal bio-oil | Improved stability and HHV | Reduced acidity; higher HHV | [8,83,84] |
| Microalgal Species | Wastewater Type | Nitrogen Removal (%) | Phosphorus Removal (%) | Biomass Productivity (g/L/day) | References |
|---|---|---|---|---|---|
| Chlorella vulgaris | Municipal wastewater | 85–92 | 78–82 | 0.35–0.45 | [96] |
| Scenedesmus obliquus | Domestic wastewater | 80–88 | 70–76 | 0.30–0.40 | [97] |
| Auxenochlorella protothecoides | Industrial effluents | 75–85 | 65–70 | 0.28–0.38 | [100] |
| Ankistrodesmus falcatus | Agro-industrial wastewater | 82–90 | 73–79 | 0.32–0.44 | [101] |
| Dunaliella tertiolecta | Synthetic nutrient medium | 88–91 | 77–83 | 0.36–0.47 | [102] |
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Bolatkhan, K.; Kakimova, A.B.; Zayadan, B.K.; Kabayeva, A.; Sandybayeva, S.K.; Dauletova, A.A.; Tomo, T. Bio-Oil from Phototrophic Microorganisms: Innovative Technologies and Strategies. BioTech 2026, 15, 11. https://doi.org/10.3390/biotech15010011
Bolatkhan K, Kakimova AB, Zayadan BK, Kabayeva A, Sandybayeva SK, Dauletova AA, Tomo T. Bio-Oil from Phototrophic Microorganisms: Innovative Technologies and Strategies. BioTech. 2026; 15(1):11. https://doi.org/10.3390/biotech15010011
Chicago/Turabian StyleBolatkhan, Kenzhegul, Ardak B. Kakimova, Bolatkhan K. Zayadan, Akbota Kabayeva, Sandugash K. Sandybayeva, Aliyam A. Dauletova, and Tatsuya Tomo. 2026. "Bio-Oil from Phototrophic Microorganisms: Innovative Technologies and Strategies" BioTech 15, no. 1: 11. https://doi.org/10.3390/biotech15010011
APA StyleBolatkhan, K., Kakimova, A. B., Zayadan, B. K., Kabayeva, A., Sandybayeva, S. K., Dauletova, A. A., & Tomo, T. (2026). Bio-Oil from Phototrophic Microorganisms: Innovative Technologies and Strategies. BioTech, 15(1), 11. https://doi.org/10.3390/biotech15010011

