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Hydrocarbon fuels from vegetable oils via hydrolysis and thermo-catalytic decarboxylation
► Converting vegetable oil into hydrocarbon fuel using hydrolysis and decarboxylation. ► The free fatty acid conversion from hydrolysis has yielded at 99.7%. ► The decarboxylation average rate was determined as 15.5mmoles/min. ► The cold flow properties of the fuel was improved using isomerization p...
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Published in: | Fuel (Guildford) 2012-05, Vol.95, p.622-629 |
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Main Authors: | , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | ► Converting vegetable oil into hydrocarbon fuel using hydrolysis and decarboxylation. ► The free fatty acid conversion from hydrolysis has yielded at 99.7%. ► The decarboxylation average rate was determined as 15.5mmoles/min. ► The cold flow properties of the fuel was improved using isomerization process.
Conversion of canola oil to normal alkane hydrocarbons was investigated using sequential reactions: continuous thermal hydrolysis and fed-batch thermo-catalytic decarboxylation. The free fatty acid (FFA) intermediate product from hydrolysis was quantified using GC–FID, which showed 99.7% conversion and the following components: palmitic, oleic, linoleic, linolenic, stearic, arachidic and behenic acids. The FFA was saturated then decarboxylated at an average rate of 15.5mmoles/min using a 5% Pd/C catalyst at 300°C. Approximately 90% decarboxylation conversion to n-alkanes was achieved within 5h of the reaction. The resulting mixture of n-alkanes can be readily converted into renewable diesel using isomerization to improve the cold flow properties of the fuel. |
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ISSN: | 0016-2361 1873-7153 |
DOI: | 10.1016/j.fuel.2011.12.041 |