Understanding the relationship between catalytic pyrolysis conditions and hydrogen production by aqueous phase reforming of the water-soluble fractions of bio-oils

• Severe catalytic pyrolysis conditions increase H 2 production in APR of AFB. • Higher H 2 production for levoglucosan-rich AFBs with low acid and ketone proportion. • 40 % H 2 production increases by adding 0.04 wt% formic acid to AFB. • The catalyst was reasonably stable over three consecutive reaction cycles. • Cumulative adsorption of heavy compounds and oligomers on the catalyst surface. The valorization to H 2 of real aqueous fractions of bio-oil (AFBs) from catalytic pyrolysis of woodchips was carried out by aqueous phase reforming (APR). Notable gas yield (23 mmol/gTOC o ) and H 2 concentration (46 mol%) were achieved, with values among the best published for the APR of real biorefinery streams. The reforming of AFBs was favoured by a high concentration of levoglucosan and low proportion of acids and ketones, with acetone and acetic acid being the most refractory compounds to APR. Relationships between the pyrolysis conditions and the H 2 production obtained by APR were assessed, with more favourable results when the pyrolysis was carried out under the most severe conditions of those studied, i.e. 0.30 catalyst/biomass ratio and 500 °C in the catalytic step. H 2 production increased to 32 mmol/gTOC o when 0.04 wt% formic acid was added to the reaction medium, showing that this strategy can overcome the low reforming ability of some AFB components. The Pt catalyst showed good stability after 3 consecutive reaction cycles, displaying only a slight decrease in TOC conversion and CCgas, but a moderate decrease in H 2 production and gas concentration. The loss of activity was ascribed to cumulative adsorption of high molecular weight compounds and oligomers on the catalyst surface.

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Publication Details

Journal
Energy Conversion and Management
Published
2024-09-05
DOI
https://doi.org/10.1016/j.enconman.2024.118999
Citations
6
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
1.11

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article

Understanding the relationship between catalytic pyrolysis conditions and hydrogen production by aqueous phase reforming of the water-soluble fractions of bio-oils

L. Calvo, J.A. Baeza, Javier Fermoso, F. G. DE LAS HERAS et al.
6 citations
Energy Conversion and Management
Thermochemical Biomass Conversion Processes
1.11
article

Understanding the relationship between catalytic pyrolysis conditions and hydrogen production by aqueous phase reforming of the water-soluble fractions of bio-oils

L. Calvo, J.A. Baeza, Javier Fermoso, F. G. DE LAS HERAS, Miguel Á. Gilarranz, Jéssica Justicia, Inés Moreno
article en
6 citations

Abstract

• Severe catalytic pyrolysis conditions increase H 2 production in APR of AFB. • Higher H 2 production for levoglucosan-rich AFBs with low acid and ketone proportion. • 40 % H 2 production increases by adding 0.04 wt% formic acid to AFB. • The catalyst was reasonably stable over three consecutive reaction cycles. • Cumulative adsorption of heavy compounds and oligomers on the catalyst surface. The valorization to H 2 of real aqueous fractions of bio-oil (AFBs) from catalytic pyrolysis of woodchips was carried out by aqueous phase reforming (APR). Notable gas yield (23 mmol/gTOC o ) and H 2 concentration (46 mol%) were achieved, with values among the best published for the APR of real biorefinery streams. The reforming of AFBs was favoured by a high concentration of levoglucosan and low proportion of acids and ketones, with acetone and acetic acid being the most refractory compounds to APR. Relationships between the pyrolysis conditions and the H 2 production obtained by APR were assessed, with more favourable results when the pyrolysis was carried out under the most severe conditions of those studied, i.e. 0.30 catalyst/biomass ratio and 500 °C in the catalytic step. H 2 production increased to 32 mmol/gTOC o when 0.04 wt% formic acid was added to the reaction medium, showing that this strategy can overcome the low reforming ability of some AFB components. The Pt catalyst showed good stability after 3 consecutive reaction cycles, displaying only a slight decrease in TOC conversion and CCgas, but a moderate decrease in H 2 production and gas concentration. The loss of activity was ascribed to cumulative adsorption of high molecular weight compounds and oligomers on the catalyst surface.

Energy Conversion and ManagementVol. 320
Universidad Rey Juan Carlos (ES), IMDEA Energy Institute (ES), Universidad Autónoma de Madrid (ES)
Comunidad de Madrid, Ministerio de Ciencia, Innovación y Universidades, European Commission, Ministerio de Ciencia e Innovación, Seventh Framework Programme, Seventh Framework Programme
Clean water and sanitation
Openalex Percentile: Top 25%
Thermochemical Biomass Conversion Processes
1.11
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