Deoxygenation of dodecanoic acid under inert atmosphere

被引:77
作者
Bernas, Heidi [1 ]
Eranen, Kari [1 ]
Simakova, Irina [1 ,2 ]
Leino, Anne-Riikka [3 ]
Kordas, Krisztian [3 ]
Myllyoja, Jukka [4 ]
Maki-Arvela, Paivi [1 ]
Salmi, Tapio [1 ]
Murzin, Dmitry Yu. [1 ]
机构
[1] Abo Akad Univ, Proc Chem Ctr, Lab Ind Chem & React Engn, FI-20500 Turku, Finland
[2] Boreskov Inst Catalysis, RU-630090 Novosibirsk, Russia
[3] Univ Oulu, EMPART Res Grp Infotech Oulu, Microelect & Mat Phys Labs, FI-90014 Oulu, Finland
[4] Neste Oil Oyj, Ctr Technol, FI-06101 Porvoo Borga, Finland
基金
芬兰科学院;
关键词
Deoxygenation; Decarboxylation; Fatty acid; Palladium; Carbon; CATALYTIC DEOXYGENATION; DIESEL FUEL; STEARIC-ACID; FATTY-ACIDS; DECARBOXYLATION; PD;
D O I
10.1016/j.fuel.2009.11.006
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
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 degrees C. The influence of reaction conditions, such as reaction temperature (300-360 degrees 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. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2033 / 2039
页数:7
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