Gerardo Gómez Millán

Dr. Gerardo Gómez Millán

Aalto University School of Chemical Engineering, Department of Bioproducts and BiosystemsPaper Converting and Packaging, Vuorimiehentie 1 , 02150 Espoo, Finland
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orcid

Research Focus & Metrics

Academic Career Length

9Years (2018-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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21 February 2019 in ChemCatChem
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Journal Article
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GMGerardo Gómez Millán
Gerardo Gómez Millán
SHSanna Hellsten
Sanna Hellsten
JLJordi Llorca
Jordi Llorca
Rafael LuqueRafael Luque
Rafael Luque
HSHerbert Sixta
Herbert Sixta
ABAlina Balu
Alina Balu

1 April 2019 in Journal of Industrial and Engineering Chemistry
Verified
Journal Article
Closed access
GMGerardo Gómez Millán
Gerardo Gómez Millán
SHSanna Hellsten
Sanna Hellsten
AKAlistair W.T. King
Alistair W.T. King
JPJuha-Pekka Pokki
Juha-Pekka Pokki
JLJordi Llorca
Jordi Llorca
HSHerbert Sixta
Herbert Sixta

1 September 2019 in Applied Catalysis A: General
Verified
Journal Article
Closed access
GMGerardo Gómez Millán
Gerardo Gómez Millán
JPJosphat Phiri
Josphat Phiri
MMMikko Mäkelä
Mikko Mäkelä
TMThad Maloney
Thad Maloney
ABAlina M. Balu
Alina M. Balu
HSHerbert Sixta
Herbert Sixta

23 September 2020 in Catalysts
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Journal Article
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GMGerardo Gómez Millán
Gerardo Gómez Millán
HSHerbert Sixta
Herbert Sixta
In the pursuit of establishing a sustainable biobased economy, valorization of lignocellulosic biomass is increasing its value as a feedstock. Nevertheless, to achieve the integrated biorefinery paradigm, the selective fractionation of its complex matrix to its single constituents must be complete. This review presents and examines the novel catalytic pathways to form furfuryl alcohol (FuOH) from xylose in a one-pot system. This production concept takes on chemical, thermochemical and biochemical transformations or a combination of them. Still, the bulk of the research is targeted to develop heterogeneous catalytic systems to synthesize FuOH from furfural and xylose. The present review includes an overview of the economic aspects to produce this platform chemical in an industrial manner. In the last section of this review, an outlook and summary of catalytic processes to produce FuOH are highlighted.

8 April 2020 in Biomass Conversion and Biorefinery
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Journal Article
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PDF file
GMGerardo Gómez Millán
Gerardo Gómez Millán
RARahul Prasad Bangalore Ashok
Rahul Prasad Bangalore Ashok
POPekka Oinas
Pekka Oinas
JLJordi Llorca
Jordi Llorca
HSHerbert Sixta
Herbert Sixta
Furfural has been highlighted as one of the top ten most rewarding bio-based building blocks by the US Department of Energy. In this study, furfural was produced from xylose and birch hydrolysate liquor employing a batch reactor in a biphasic system. The formation of furfural was conducted under auto-catalyzed conditions. 2-sec-Butylphenol was used as extractant to promptly extract furfural from the aqueous phase in order to minimize furfural degradation reactions. The effect of time, temperature, and organic-to-aqueous phase ratio were investigated. The maximum furfural yields from xylose and birch hydrolysate liquor as feedstock under auto-catalyzed conditions when employing 2-sec-butylphenol (SBP) were 59 mol% and 54 mol%, respectively. In the monophasic system when using hydrolysate, 46% furfural was yielded. Based on a techno-economic analysis carried out for furfural, the total investment cost for a plant integrated with an existing pulp mill or bio-refinery is estimated as 14 M€. The minimum selling price of furfural found to be 1.62 € kg−1. With a furfural selling price of 1.93 € kg−1, the payback period is approximately 5 years and an internal rate of return (IRR) of 20.7% is achieved at the end of the project lifetime.

1 December 2018 in Fuel Processing Technology
Verified
Journal Article
Open access
GMGerardo Gómez Millán
Gerardo Gómez Millán
ZAZouhair El Assal
Zouhair El Assal
KNKaarlo Nieminen
Kaarlo Nieminen
SHSanna Hellsten
Sanna Hellsten
JLJordi Llorca
Jordi Llorca
HSHerbert Sixta
Herbert Sixta