2019
DOI: 10.3390/app9112386
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Conversion of Stearic Acid into Bio-Gasoline over Pd/ZSM-5 Catalysts with Enhanced Accessibility

Abstract: Palladium supported on nanocrystalline ZSM-5 (n-ZSM-5, Si/Al = 32) and hierarchical ZSM-5 (h-ZSM-5) with different acidity (Si/Al = 33, 51, 122) were tested in the liquid-phase conversion of stearic acid under nitrogen atmosphere (6 bar). The incorporation of Pd into ZSM-5 zeolite increased significantly the share of gasoline in the reaction products due to the promotion by this metal of both decarboxylation and hydrogen transfer reactions. Likewise, the Pd nanoparticles dispersed over the zeolitic support fav… Show more

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Cited by 4 publications
(6 citation statements)
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“…It is also noteworthy that, in an experiment carried out at 250 °C under the same experimental conditions and catalyst [Pd/h-ZSM-5 (122)] but adding 6 bar of nitrogen instead of hydrogen, the conversion decreased abruptly from 61 to 6%. 72 This result bears out the role of hydrogen in activating palladium sites for DC. On the basis of these results, a Energy & Fuels temperature of 250 °C was selected for further studies to limit the extension of cracking reactions and favor the stearic acid DC while still keeping a significant catalytic activity (conversion over 60%).…”
Section: Resultsmentioning
confidence: 67%
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“…It is also noteworthy that, in an experiment carried out at 250 °C under the same experimental conditions and catalyst [Pd/h-ZSM-5 (122)] but adding 6 bar of nitrogen instead of hydrogen, the conversion decreased abruptly from 61 to 6%. 72 This result bears out the role of hydrogen in activating palladium sites for DC. On the basis of these results, a Energy & Fuels temperature of 250 °C was selected for further studies to limit the extension of cracking reactions and favor the stearic acid DC while still keeping a significant catalytic activity (conversion over 60%).…”
Section: Resultsmentioning
confidence: 67%
“…Taking into account that the three catalysts show a similar Pd content (∼1 wt %), it is concluded that the transformation of the fatty acid also depends heavily upon the acidity of the MFI support. Additionally, the same experiment carried out using Pd supported over a commercial ZSM-5 (Pd/n-ZSM-5), which shows a Si/Al atomic ratio of 32 and whose physicochemical properties may be found elsewhere, 72 pointed out a distinctly lower conversion (33%) than the equivalent Pd/h-ZSM-5 (33) (71%), while its selectivity toward C 13 −C 18 hydrocarbons was 94%, slightly higher than the 82% value attained over Pd/h-ZSM-5 (33). These results prove the advantage of using a hierarchical ZSM-5 support, because its better accessibility facilitates not only cracking but DC reactions as well, leading to a rather enhanced catalytic activity.…”
Section: Resultsmentioning
confidence: 99%
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“…32,33,34 In that context of emergence of new zeolitetype materials such as hierarchical zeolites it appears very important to identify the influence of the morphology on the formation and evolution of CSS. 25,35,36,37,38 MFI-type zeolite is particularly interesting due to its three-dimensional channel system with 10-membered ring (MR) openings (0.55-0.56 nm). Thanks to new synthesis methods, [27][28][29][30][39][40][41][42][43] it is now possible to control the morphology of zeolites to eventually make their properties "tunable" not only by preparing materials in the form of microcrystals but also with more complex architectures.…”
Section: Introductionmentioning
confidence: 99%