A cascade biorefinery for the valorization of microalgal biomass: biodiesel, biogas, fertilizers and high valuable compounds

被引:29
作者
Monlau, F. [1 ]
Suarez-Alvarez, S. [2 ]
Lallement, A. [1 ]
Vaca-Medina, G. [3 ,4 ]
Giacinti, G. [3 ,4 ]
Munarriz, M. [5 ]
Urreta, I [2 ]
Raynaud, C. [3 ,4 ]
Ferrer, C. [1 ]
Castanon, S. [2 ]
机构
[1] APESA, Pole Valorisat, Cap Ecol, Ave Freder Joliot Curie, F-64230 Lescar, France
[2] Neiker Basque Inst Agr Res & Dev, Basque Res & Technol Alliance BRTA, Dept Plant Prod & Protect, 104,Km 355, E-01192 Arkaute, Spain
[3] Univ Toulouse, Lab Chim Agroind, LCA, INRAE, Toulouse, France
[4] Univ Toulouse, INPT, Ctr Applicat & Traitement Agroressources CATAR, Toulouse, France
[5] Natl Renewable Energy Ctr CENER, Biomass Dept, C Ciudad Innovac 7, Navarra 31621, Spain
来源
ALGAL RESEARCH-BIOMASS BIOFUELS AND BIOPRODUCTS | 2021年 / 59卷
关键词
Anaerobic digestion; Amino acids; Biorefinery; Chlorella protothecoides; Enzymatic hydrolysis; Saponification; LIPID EXTRACTED RESIDUES; ANAEROBIC-DIGESTION; CHLORELLA-PROTOTHECOIDES; CO-DIGESTION; DIRECT SAPONIFICATION; METHANE YIELD; WASTE; PRETREATMENT; SOLVENT; CONVERSION;
D O I
10.1016/j.algal.2021.102433
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Bio-refining of algal biomass is currently considered as a key strategy to cut down the cost and improve the overall feasibility of algal-derived biodiesel. With that aim, in this study it was implemented a three-stage biorefinery process for the recovery of five differentiated bio-products from heterotrophically Chlorella protothecoides biomass. In the first stage, which was conducted at pilot scale from 14 kg of wet biomass, direct saponification converted 40% of dry algal biomass into free fatty acids. The obtained fatty acids were successfully turned into high quality biodiesel, whereas the analysis of unsaponifiables revealed the presence of interesting high-value biomolecules such as sterols (62%), squalene and carotenoids (1.7% each). The de-oiled biomass underwent an enzymatic hydrolysis process. This second process led to the valorization of 9% (0.09 kg/kg) of the remaining algal components which were recovered in a liquid hydrolysate mainly composed of soluble amino acids (15 g/L) and sugars (27.9 g/L). In the last biorefinery stage, the leftover solid fraction after enzymatic hydrolysis (0.36 kg/kg) was used as substrate in an anaerobic digestion process which yielded biogas at 196 +/- 4 NL CH4/kg VS. The digestate co-produced in this stage was chemically characterized and assessed as fertilizer (at a dose of 170kg N/ha) for wheat and tomato plant growth, with comparable effect to that of industrial fertilizers. This use allowed a closed-loop system through the recycling of nutrients for primary production. The exposed cascade-processing, which was demonstrated technically feasible, could potentially improve the value of algal biomass through the production of multiple products.
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页数:11
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