Reactions of furfural and acetic acid as model compounds for bio-oil upgrading in supercritical ethanol

Author(s):  
Jun Wang ◽  
Zhongyang Luo ◽  
Jixiang Zhang ◽  
Qi Dang ◽  
Wen Chen
BioResources ◽  
2013 ◽  
Vol 8 (3) ◽  
Author(s):  
Wen Chen ◽  
Zhongyang Luo ◽  
Yi Yang ◽  
Guoxiang Li ◽  
Jixiang Zhang ◽  
...  

2016 ◽  
Vol 177 ◽  
pp. 579-590 ◽  
Author(s):  
G. Esteban-Díez ◽  
María V. Gil ◽  
C. Pevida ◽  
D. Chen ◽  
F. Rubiera

2014 ◽  
Vol 39 (32) ◽  
pp. 18675-18687 ◽  
Author(s):  
Shurong Wang ◽  
Qinjie Cai ◽  
Fan Zhang ◽  
Xinbao Li ◽  
Li Zhang ◽  
...  

ACS Omega ◽  
2019 ◽  
Vol 4 (25) ◽  
pp. 21516-21528 ◽  
Author(s):  
Santiago Gutiérrez-Rubio ◽  
Inés Moreno ◽  
David P. Serrano ◽  
Juan M. Coronado

2020 ◽  
Vol 7 (1) ◽  
pp. 29-36
Author(s):  
Antonina A. Stepacheva ◽  
Mariia E. Markova ◽  
Yury V. Lugovoy ◽  
Kirill V. Chalov ◽  
Mikhail G. Sulman ◽  
...  

AbstractHydrotreatment of bio-oil oxygen compounds allows the final product to be effectively used as a liquid transportation fuel from biomass. Deoxygenation is considered to be one of the most promising ways for bio-oil upgrading. In the current work, we describe a novel approach for the deoxygenation of bio-oil model compounds (anisole, guaiacol) using supercritical fluids as both the solvent and hydrogen-donors. We estimated the possibility of the use of complex solvent consisting of non-polar n-hexane with low critical points (Tc = 234.5 ºC, Pc = 3.02 MPa) and propanol-2 used as H-donor. The experiments were performed without catalysts and in the presence of noble and transition metals hydrothermally deposited on the polymeric matrix of hypercrosslinked polystyrene (HPS). The experiments showed that the presence of 20 vol. % of propanol-2 in n-hexane results in the highest (up to 99%) conversion of model compounds. When the process was carried out without a catalyst, phenols were found to be a major product yielding up to 95 %. The use of Pd- and Co-containing catalyst yielded 90 % of aromatic compounds (benzene and toluene) while in the presence of Ru and Ni cyclohexane and methylcyclohexane (up to 98 %) were the main products.


2019 ◽  
Vol 377 ◽  
pp. 120144 ◽  
Author(s):  
A.R. Costa da Cruz ◽  
J.J. Verstraete ◽  
N. Charon ◽  
J.-F. Joly

2019 ◽  
Vol 49 (4) ◽  
pp. 297-302
Author(s):  
Yanina P. Maidana ◽  
Eduardo Izurieta ◽  
Andres I. Casoni ◽  
Maria A. Volpe ◽  
Eduardo Lopez ◽  
...  

This work focuses on the study of hydrogen production process departing from waste lignocellulosic biomass. The bio-oil was first obtained by non-catalytic fast pyrolysis of sunflower seed hulls. Subsequently, it was upgraded to reduce the concentration of higher molecular weight compounds by water addition and mixing. A 1/1 bio-oil:water ratio was selected here. Later, a thermodynamic analysis based on free energy minimization was profited to study the steam reforming process of the upgraded bio-oil sample. The influence of the operation temperature on the reforming was analyzed. The highest hydrogen yields were obtained at ~740°C. A comparison with acetic acid used as model compound of the bio-oil is included. Results show that acetic acid is not a good approximation of a real aqueous phase of upgraded bio oil fraction. The study concludes with an analysis on the energetic efficiency, showing that its maximum is presented at lower temperatures than the maximum yield, due to the thermal requirements of preheating.


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