Heterogeneous Catalysts in the Dehydration of Fructose to HMF

Wednesday, October 19, 2011: 1:20 PM
208 C (Minneapolis Convention Center)
Sylvia Reiche1, Xiao Chen Zhao2, Klaus Friedel3, Matthew Aronson4, Raoul Blume5, Edward Kunkes1, Jean-Philippe Tessonnier6, Malte Behrens1, Dangsheng Su1, Robert J. Davis7 and Robert Schlögl1, (1)Inorganic Chemistry, Fritz Haber Institute of the Max Planck Society, Berlin, Germany, (2)Fritz Haber Institute of the Max Planck Society, Berlin, Germany, (3)Fritz Haber Institute of the Max Planck Society, 14195 Berlin, Germany, (4)Dept. of Chemical Engineering, Univ. of California, Santa Barbara, Santa Barbara, CA, (5)Helmholtz-Zentrum Berlin für Materialien und Energie, D-12489 Berlin, Germany, (6)Department of Chemical Engineering, University of Delaware, Newark, DE, (7)Chemical Engineering, University of Virginia, Charlottesville, VA

Several crucial steps in the upgrading of biomass-derived raw materials involve acid catalyzed reactions, such as the hydrolysis of cellulose or the dehydration of sugars. Although heterogeneous catalysts are desired in large scale industrial processes, their application is limited by several challenges concerning the conversion of these highly functionalized feedstocks.

In our work, we tested a wide range of heterogeneous acids for the dehydration of fructose into 5-hydroxymethyl furfural (HMF) in 2-butanol solvent. The main focus was on carbon based catalysts, due to their structural diversity and hydrothermal stability. The amount of acidic functional groups determined by titration varied with the carbon support between 0.1 mmol/g for functionalized multi-walled carbon nanotubes (MWCNTs) and 1.7 mmol/g for amorphous carbon prepared by glucose pyrolysis (AGP). However, tests involving exposure of the catalyst to heated reaction solvent showed that part of the acidic groups is released in the solution (i. e. leaching) and the reaction is subsequently catalyzed at least partly homogeneously. The described leaching phenomenon was observed for all materials tested, including polymer resins, such as Nafion and Amberlyst. In case of functionalized AGP, the system retained 0.42 mmol/g of acid functional groups after four consecutive pretreatments in reaction solvent (2-butanol) at reaction temperature (130°C). 

A second aspect of catalyst deactivation is the surface poisoning by secondary polymerization products, i. e. humins. This phenomenon was further investigated by comparing the activity towards dehydration of fructose with activities in a reference reaction, i. e. the esterification of acetic acid with ethanol. The esterification reaction was chosen because this reaction does not show deactivation due to secondary products. Although some systems, such as the pretreated AGP catalyst, were stable and recyclable in the esterification reaction, they significantly deactivated already after the first reaction run of fructose dehydration. The accumulation of secondary polymerization products on the catalyst surface was observed by inter alia scanning electron microscopy (SEM).

In conclusion, different deactivation mechanisms were identified for the use of heterogeneous catalysts in the dehydration of fructose. The leaching of functional groups can be suppressed by suitable pretreatments of the catalysts. Adsorption studies suggest that solvent choice can influence the extent of humin accumulation. However, a thorough recycling requires calcinable, hydrothermally stable catalysts.

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See more of this Session: Catalytic Biomass Conversion to Chemicals I
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