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Oleaginous yeast platform for producing biofuels via co-solvent hydrothermal liquefaction

BACKGROUND: Oleaginous microorganisms are attractive feedstock for production of liquid biofuels. Direct hydrothermal liquefaction (HTL) is an efficient route that converts whole, wet biomass into an energy-dense liquid fuel precursor, called ‘biocrude’. HTL represents a promising alternative to con...

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Detalles Bibliográficos
Autores principales: Jena, Umakanta, McCurdy, Alex T., Warren, Andrew, Summers, Hailey, Ledbetter, Rhesa N., Hoekman, S. Kent, Seefeldt, Lance C., Quinn, Jason C.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: BioMed Central 2015
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4605089/
https://www.ncbi.nlm.nih.gov/pubmed/26468320
http://dx.doi.org/10.1186/s13068-015-0345-5
Descripción
Sumario:BACKGROUND: Oleaginous microorganisms are attractive feedstock for production of liquid biofuels. Direct hydrothermal liquefaction (HTL) is an efficient route that converts whole, wet biomass into an energy-dense liquid fuel precursor, called ‘biocrude’. HTL represents a promising alternative to conventional lipid extraction methods as it does not require a dry feedstock or additional steps for lipid extraction. However, high operating pressure in HTL can pose challenges in reactor sizing and overall operating costs. Through the use of co-solvents the HTL operating pressure can be reduced. The present study investigates low-temperature co-solvent HTL of oleaginous yeast, Cryptococcus curvatus, using laboratory batch reactors. RESULTS: In this study, we report the co-solvent HTL of microbial yeast biomass in an isopropanol–water binary system in the presence or absence of Na(2)CO(3) catalyst. This novel approach proved to be effective and resulted in significantly higher yield of biocrude (56.4 ± 0.1 %) than that of HTL performed without a co-solvent (49.1 ± 0.4 %)(p = 0.001). Addition of Na(2)CO(3) as a catalyst marginally improved the biocrude yield. The energy content of the resulting biocrude (~37 MJ kg(−1)) was only slightly lower than that of petroleum crude (42 MJ kg(−1)). The HTL process was successful in removing carboxyl groups from fatty acids and creating their associated straight-chain alkanes (C(17)–C(21)). Experimental results were leveraged to inform techno-economic analysis (TEA) of the baseline HTL conversion pathway to evaluate the commercial feasibility of this process. TEA results showed a renewable diesel fuel price of $5.09 per gallon, with the HTL-processing step accounting for approximately 23 % of the total cost for the baseline pathway. CONCLUSIONS: This study shows the feasibility of co-solvent HTL of oleaginous yeast biomass in producing an energy-dense biocrude, and hence provides a platform for adding value to the current dairy industry. Co-solvents can be used to lower the HTL temperature and hence the operating pressure. This process results in a higher biocrude yield at a lower HTL temperature. A conceptual yeast HTL biofuel platform suggests the use of a dairy waste stream for increasing the productivity and sustainability of rural areas while providing a new feedstock (yeast) for generating biofuels. ELECTRONIC SUPPLEMENTARY MATERIAL: The online version of this article (doi:10.1186/s13068-015-0345-5) contains supplementary material, which is available to authorized users.