Cited by 174Algal biology and biofuel productionThermochemical Biomass Conversion ProcessesCatalysis and Hydrodesulfurization Studies

Hydrothermal Liquefaction of Low Lipid Content Microalgae into Bio-Crude Oil

G. Yu, Y. Zhang, L. Schideman, T. L. Funk, Z. Wang·2011·Transactions of the ASABE

Abstract

Microalgae have attracted significant attention in biofuel research over recent years because of their rapid photosynthetic growth rates and the high lipid content achieved with certain species and culturing conditions. Most past research has focused on high-lipid algal species and increasing the lipid content in order to extract these lipids for conventional transesterification to biodiesel. High-lipid algae and the associated culturing conditions have often resulted in lower biomass productivities, thus limiting the potential yield of algae-based biofuel. An alternative approach is to culture fast-growing low-lipid algae and then convert the resulting biomass into bio-crude oil through a hydrothermal liquefaction (HTL) process. This article presents results for producing bio-crude oil via HTL conversion of Chlorella pyrenoidosa, a common fast-growing green microalgae species with low lipid content. The products of the HTL conversion generally self-separate into three phases: a gaseous product, an aqueous phase product, and bio-crude oil product. For the purpose of this study, a toluene-soluble fraction of the raw oil product was defined as refined oil. The natural phase-separation of HTL products is highly advantageous for algal biofuel production because it minimizes energy input for dewatering. To help optimize the HTL process, the effects of key operating parameters (initial pressure, reaction temperature, and reaction time) on the oil product yields were investigated. The experimental results indicate that reaction temperature and reaction time can greatly affect the refined oil yield. The initial pressure provided by nitrogen had little effect on oil yield. The highest refined oil yield was 39.4% 1.2% of the total dry mass of algal feedstock, which was achieved at 280C reaction temperature with 120 min reaction time.

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Crossref · 10.13031/2013.36241

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Authors
Yu, G., Zhang, Y., Schideman, L., Funk, T. L., & Wang, Z.
Affiliations
University of Illinois Urbana-Champaign (US)
Venue
Transactions of the ASABE
Published
2011
Volume
54
Issue
1
Pages
239-246
ISSN
  • 2151-0032 (ISSN-L)
  • 2151-0040
OpenAlex
W2064339781
Cited by
174
References
0
Citations by year
2026: 4 · 2025: 6 · 2024: 9 · 2023: 3 · 2022: 13 · 2021: 11 · 2020: 7 · 2019: 19 · 2018: 14 · 2017: 15 · 2016: 18 · 2015: 19 · 2014: 13 · 2013: 15 · 2012: 7
FWCI
4.79
Type
journal article
Language
en
Open access
closed
Locations
Transactions of the ASABE (publishedVersion)
Topics
  • Physical Sciences › Energy › Renewable Energy, Sustainability and the Environment › Algal biology and biofuel production
  • Physical Sciences › Engineering › Biomedical Engineering › Thermochemical Biomass Conversion Processes
  • Physical Sciences › Engineering › Mechanical Engineering › Catalysis and Hydrodesulfurization Studies
Keywords
hydrothermal liquefaction, Chlorella pyrenoidosa, bio-crude oil, algal biofuels, phase separation, reaction temperature, reaction time (chemistry), initial pressure, oil yield, nitrogen pressure

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