Bio-oil production by catalytic solvent liquefaction from a wild microalgae consortium

被引:0
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作者
Oscar D. González-Gálvez
Isaac Nava Bravo
Rogelio Cuevas-García
Sharon B. Velásquez-Orta
Adam P. Harvey
Luis Cedeño Caero
María Teresa Orta Ledesma
机构
[1] Instituto de Energías Renovables,Coordinación de Ingeniería Ambiental, Instituto de Ingeniería
[2] UNAM,Unidad de Investigaciones en Catálisis (UNICAT), Departamento de Ingeniería Química, Facultad de Química
[3] Universidad Nacional Autónoma de México,School of Chemical Engineering
[4] Ciudad Universitaria,undefined
[5] Universidad Nacional Autónoma de México,undefined
[6] Ciudad Universitaria,undefined
[7] Newcastle University,undefined
来源
关键词
Native microalgae biomass; Bio-oil; Catalytic solvent liquefaction; Zeolite HZSM-5; Tetralin;
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学科分类号
摘要
Due to the increase in greenhouse gas emissions by combustion of fossil fuels, new alternatives for obtaining clean energy have been investigated. In this work, a wild microalgae consortium, grown in treated wastewater, was used to produce bio-oil by catalytic solvent liquefaction process. Tetralin and zeolite HZSM-5 (Si/Al = 80) were employed as a reaction medium and catalyst, respectively. The effect of H2 pressure and reaction time on biocrude yield, conversion of biomolecules, and the type of generated chemical compounds in the bio-oil were investigated, and reaction schemes were proposed. The best reaction condition was at 120 min and 760 psi, where a bio-oil yield of 51 wt% was obtained and high percentage of the original protein content was converted. The main type of compounds in the produced bio-oil were oxygenated (~ 50 chromatographic area %) and nitrogenated (~ 18 area %) compounds. H2 pressure is an important variable to process proteins, lipids, and simple carbohydrates. Despite the high protein content in the feedstock, a relatively low nitrogen content of 1.2–1.5 wt% was found in the resultant bio-oil, which has an estimated HHV of 32–33 MJ/kg.
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页码:2627 / 2639
页数:12
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