4.7 Article

Valorisation of harmful algae bloom (Enteromorpha prolifera) for polysaccharide and crude bio-oil production

期刊

FUEL
卷 324, 期 -, 页码 -

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2022.124482

关键词

Algal bloom; Polysaccharide extraction; Hydrothermal liquefaction; Crude bio-oil; Integrated biorefinery

资金

  1. Minjiang University, Fujian Education Department-Young and Middle-aged Teachers Funding [JT180409]
  2. Fujian Province Key Laboratory for the Development of Bioactive Material from Marine Algae [2018FZSK06]
  3. National Natural Science Foundation of China [31801606]

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This study extracted water-soluble polysaccharide from excessive growth of Enteromorpha prolifera (EP) and utilized residual EP to generate crude bio-oil using hydrothermal liquefaction (HTL). The study found optimal conditions for polysaccharide extraction and successfully co-liquefied residual EP with microalgae. The valorisation route developed in this study is important for full utilization of EP and improving its economic viability and sustainability.
The excessive growth of Enteromorpha prolifera (EP) could lead to the harmful algae bloom, making the disposal of EP (millions of tons) an inevitable problem. This study aimed to extract water-soluble polysaccharide from EP, followed by utilizing an emerging thermochemical technique (hydrothermal liquefaction, HTL) to generate crude bio-oil from residual EP. 2 (k) factorial design with replicated center points were employed to evaluate the necessity of using response surface methodology (RSM) to optimize polysaccharide extraction conditions. The curvature effect was identified to be temperature*temperature in this study, and the interaction effects (solid/ water ratio*time & temperature*time) were also crucial for EP polysaccharide extraction. The maximal polysaccharide yield of 12.1 wt% was achieved under the optimal conditions (1:55 g/mL solid/water ratio, 70 degrees C, 60 min). The polysaccharide solution acquired under the optimal conditions had a DPPH radical scavenging rate of 24.3% and reducing power of 0.28. The residual EP after polysaccharide extraction was commonly discarded as waste, which was used as HTL feedstock for biocrude production in this study. HTL of residual EP resulted in a biocrude yield of 26.6 wt%, dry-ash free (daf) and a hydro-char yield of 22.4 wt%, daf, which were comparable with that of raw EP, suggesting the viability of obtaining value-added polysaccharide and biocrude simultaneously. We also co-liquified residual EP with microalgae (Chlorella sp.) under various mixing ratios, and satisfactory biocrude yield, chemical composition, higher heating value, energy recovery, and carbon recovery were achieved. The valorisation route developed in this study is of importance for full utilization of EP, thereby improving the economic viability and sustainability for EP biorefinery.

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