Catalytic Deoxygenation of Stearic Acid in a Continuous Reactor over a Mesoporous Carbon-Supported Pd Catalyst

Lestari, S., Maki-Arvela, P., Bernas, H., Simakova, O., Sjoholm, R., Beltramini, J., Lu, G. Q., Myllyoja, J., Simakova, I. and Murzin, D. Y. (2009) Catalytic Deoxygenation of Stearic Acid in a Continuous Reactor over a Mesoporous Carbon-Supported Pd Catalyst. ENERGY & FUELS, 23 8: 3842-3845. doi:10.1021/ef900110t


Author Lestari, S.
Maki-Arvela, P.
Bernas, H.
Simakova, O.
Sjoholm, R.
Beltramini, J.
Lu, G. Q.
Myllyoja, J.
Simakova, I.
Murzin, D. Y.
Title Catalytic Deoxygenation of Stearic Acid in a Continuous Reactor over a Mesoporous Carbon-Supported Pd Catalyst
Journal name ENERGY & FUELS   Check publisher's open access policy
ISSN 0887-0624
Publication date 2009-08-01
Year available 2009
Sub-type Article (original research)
DOI 10.1021/ef900110t
Volume 23
Issue 8
Start page 3842
End page 3845
Total pages 4
Editor Klein, M. T.
Place of publication United States
Publisher American Chemical Society
Collection year 2010
Language eng
Subject C1
970109 Expanding Knowledge in Engineering
100708 Nanomaterials
Abstract Catalytic deoxygenation of neat stearic acid was studied at 360 degrees C under 10 bar argon or 5 vol % hydrogen in argon in a fixed-bed reactor (down flow) using mesoporous-supported Pd/C (Sibunit) beads as a catalyst. The results showed stable catalyst performance, giving about 15% conversion level of stearic acid. The main liquid-phase product was heptadecane, while the main gaseous products were CO and CO2.
Keyword Vegetable-oils
Diesel fuel
Decarboxylation
Q-Index Code C1
Q-Index Status Confirmed Code

 
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Created: Fri, 04 Sep 2009, 20:21:41 EST