Abstract

The gas-phase aldol condensation of propanal, taken as model for the aldehyde components in bio-oils, has been studied with a combined operando set-up allowing to perform FT-IR & UV–Vis diffuse reflectance spectroscopy (DRS) with on-line mass spectrometry (MS). The selected solid base catalysts, a cesium-exchanged X zeolite (Cs-X), a calcium hydroxyapatite (Ca-HA) and two alkaline metal-grafted ultrastable Y (Na- and Rb-USY) zeolites, were characterized ex-situ by FT-IR after CO (CO-IR) and pyridine (Py-IR) adsorption and subsequent desorption. The combined operando spectroscopy study shows that alkaline metal-grafted USY zeolites are the most selective catalysts towards aldol dimer product formation, while the hydroxyapatite was more selective for successive aldol condensation reactions. For Na-USY and Rb-USY, the C–C coupling seems to be the rate-determining step during the surface reaction, which is the limiting stage of the overall catalytic process. In contrast, for the two more basic catalysts, i.e., Cs-X and Ca-HA desorption is limiting the overall catalytic process. Furthermore, the combined operando FT-IR & UV–Vis DRS methodology allowed monitoring the formation of carbonaceous deposits as a function of reaction time. In particular, for Cs-X and Ca-HA the rapid formation of carbonaceous deposits was observed consisting of (poly-)aromatics and highly conjugated structures, respectively. The physicochemical properties of Ca-HA with strong basic sites and moderate acidity limit its deactivation despite the observed coke formation. On the other hand, both USY catalysts were more efficient in suppressing coke formation likely due to the moderate strength of their active sites.

Highlights

  • Bio-oils obtained by pyrolysis are chemically complex and do not have yet the desired characteristics of a transportation fuel [1]

  • The combined operando spectroscopy study shows that alkaline metal-grafted USY zeolites are the most selective catalysts towards aldol dimer product formation, while the hydroxyapatite was more selective for successive aldol condensation reactions

  • The activity, selectivity and stability of the solid base catalyst materials under study, namely cesium-exchanged X zeolite (Cs-X), calcium hydroxyapatite (Ca-HA), Na-USY and Rb-USY, were tested for the gas-phase aldol condensation of propanal using a combination of operando FT-IR & UV–Vis diffuse reflectance spectroscopy (DRS) measurements with on-line mass spectrometry (MS)

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Summary

Introduction

Bio-oils obtained by pyrolysis are chemically complex and do not have yet the desired characteristics of a transportation fuel [1]. A detailed operando spectroscopy study on the self-condensation of propanal, used as a model for the aldehydes found in pyrolytic bio-oils, is reported over a selection of solid base catalysts. Time-on-stream analysis of the evolution of carbonaceous species clearly shows differences in both rate and composition of these carbonaceous deposits over the different catalytic materials Both alkaline metal-grafted USY zeolites show the highest resistance against coking, which is probably related to the moderate strength of the active sites, as further confirmed by ex-situ FT-IR analysis of the catalytic solids with CO and pyridine as probe molecules for acid-base characterization. The observed differences in amount of deposited coke were corroborated with Thermogravimetric Analysis (TGA) of the spent catalyst materials

Materials
Catalyst Characterization
Carbon Monoxide FT‐IR Spectroscopy
Pyridine FT‐IR Spectroscopy
Operando FT‐IR Spectroscopy
Operando UV–Vis Diffuse Reflectance Spectroscopy
On‐Line Mass Spectrometry
Coke Amount and Composition of Spent Catalyst
Conclusions
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