Hydrothermal Co-Liquefaction of Sugarcane Bagasse and Residual Cooking Soybean Oil for Bio-Crude Production

被引:0
|
作者
Oliveira, Matheus Venancio de [1 ]
Pelisson, Maria [1 ]
Hamerski, Fabiane [1 ]
Kanda, Luis Ricardo Shigueyuki [1 ]
Voll, Fernando A. P. [1 ]
Ramos, Luiz Pereira [1 ]
Corazza, Marcos Lucio [1 ]
机构
[1] Univ Fed Parana, Dept Chem Engn, Rua Coronel Francisco Heraclito Santos 100, BR-81531980 Curitiba, PR, Brazil
关键词
bio-crude; hydrothermal co-liquefaction; ethanol; residual soybean oil; sugarcane bagasse; AQUEOUS-PHASE; ALGAL BIOMASS; SWINE MANURE; WASTE-WATER; CONVERSION; BIOCRUDE; HYDROLYSIS;
D O I
10.3390/pr12071371
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrothermal co-liquefaction (co-HTL) is a process involving two sources of biomasses aiming at bio-crude production. Since there is a lack of studies performed with sugarcane bagasse and residual soybean oil, this study investigated different conditions for the co-HTL of these biomasses, with and without the presence of ethanol as a co-solvent to maximize the bio-crude yield. All co-HTL reactions were carried out in a 300 mL Parr (R) reactor at temperatures ranging from 200 to 300 degrees C. After the reaction, a vacuum filtration was performed to separate the bio-char, later washed with ethanol to extract heavy bio-crude, while the liquid-phase was mixed with dichloromethane to recover light bio-crude. Bio-crude yields of around 95 wt.% were obtained at 300 degrees C using ethanol and water as solvents. The highest bio-char yield (16.6 wt.%) was achieved when using only sugarcane bagasse as the substrate, without the presence of soybean oil. Bio-crude samples obtained at higher temperatures (280 degrees C and 300 degrees C) using ethanol as a hydrogen donor presented higher contents of both free fatty acids and fatty acid ethyl esters. This work presents a promising process to produce high-quality bio-crude using an abundant feedstock (sugarcane bagasse) in the presence of a lipid source which could cause environmental problems if poorly handled.
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页数:15
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