TY - JOUR
T1 - Deoxygenation of dodecanoic acid under inert atmosphere
AU - Bernas, Heidi
AU - Eränen, Kari
AU - Simakova, Irina
AU - Leino, Anne-Riikka
AU - Kordás, Krisztián
AU - Myllyoja, Jukka
AU - Mäki-Arvela, Päivi
AU - Salmi, Tapio
AU - Murzin, Dmitry Yu
N1 - Copyright:
Copyright 2018 Elsevier B.V., All rights reserved.
PY - 2010/8
Y1 - 2010/8
N2 - A laboratory-scale fixed bed reactor (down-flow) was developed for the deoxygenation of dodecanoic (lauric) acid under inert atmosphere. This reaction can be utilized to produce renewable diesel components. The main products were undecane (decarboxylation) and undecene (decarbonylation). The catalysts were a palladium catalyst supported on mesoporous carbon, Sibunit (egg-shell type with spherical granules of 1.6-2.0 mm in diameter), and a commercial Pd/C catalyst. The challenge was to obtain a high activity and selectivity to undecane, as pure dodecanoic acid without any solvents was used. Moreover, the complete reactor system consisting of a reactant feed vessel, a pump, lines, a sampling valve, and a collector of the residue had to be heated, since saturated fatty acids with more than nine carbon atoms have a melting point exceeding 20 °C. The influence of reaction conditions, such as reaction temperature (300-360 °C), pressure (5-20 bar), gas flow rate, reactant concentrations, was studied. The reactant conversion increased when an inert gas (argon) flow was applied co-currently with the reactant flow. The argon pressure did not have any significant impact on the performance. The reason for the catalyst deactivation was determined to be coking.
AB - A laboratory-scale fixed bed reactor (down-flow) was developed for the deoxygenation of dodecanoic (lauric) acid under inert atmosphere. This reaction can be utilized to produce renewable diesel components. The main products were undecane (decarboxylation) and undecene (decarbonylation). The catalysts were a palladium catalyst supported on mesoporous carbon, Sibunit (egg-shell type with spherical granules of 1.6-2.0 mm in diameter), and a commercial Pd/C catalyst. The challenge was to obtain a high activity and selectivity to undecane, as pure dodecanoic acid without any solvents was used. Moreover, the complete reactor system consisting of a reactant feed vessel, a pump, lines, a sampling valve, and a collector of the residue had to be heated, since saturated fatty acids with more than nine carbon atoms have a melting point exceeding 20 °C. The influence of reaction conditions, such as reaction temperature (300-360 °C), pressure (5-20 bar), gas flow rate, reactant concentrations, was studied. The reactant conversion increased when an inert gas (argon) flow was applied co-currently with the reactant flow. The argon pressure did not have any significant impact on the performance. The reason for the catalyst deactivation was determined to be coking.
KW - Carbon
KW - Decarboxylation
KW - Deoxygenation
KW - Fatty acid
KW - Palladium
UR - http://www.scopus.com/inward/record.url?scp=77955264075&partnerID=8YFLogxK
U2 - 10.1016/j.fuel.2009.11.006
DO - 10.1016/j.fuel.2009.11.006
M3 - Article
AN - SCOPUS:77955264075
SN - 0016-2361
VL - 89
SP - 2033
EP - 2039
JO - Fuel
JF - Fuel
IS - 8
ER -