catalysts
Article
Investigation of Gas Diffusion Electrode Systems for the
Electrochemical CO
2
Conversion
Hilmar Guzmán
1,2,
*
,†
, Federica Zammillo
1,†
, Daniela Roldán
1
, Camilla Galletti
1
, Nunzio Russo
1
and Simelys Hernández
1,2,
*
Citation: Guzmán, H.; Zammillo, F.;
Roldán, D.; Galletti, C.; Russo, N.;
Hernández, S. Investigation of Gas
Diffusion Electrode Systems for the
Electrochemical CO
2
Conversion.
Catalysts 2021, 11, 482. https://
doi.org/10.3390/catal11040482
Academic Editor: Bruno Fabre
Received: 13 February 2021
Accepted: 6 April 2021
Published: 9 April 2021
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4.0/).
1
CREST Group, Department of Applied Science and Technology (DISAT), Politecnico di Torino,
C.so Duca degli Abruzzi, 24, 10129 Turin, Italy; federica.zammillo@polito.it (F.Z.);
daniela.roldan@polito.it (D.R.); camilla.galletti@polito.it (C.G.); nunzio.russo@polito.it (N.R.)
2
Center for Sustainable Future Technologies (IIT@PoliTo), IIT—Istituto Italiano di Tecnologia,
Via Livorno, 60, 10144 Turin, Italy
* Correspondence: hilmar.guzman@polito.it (H.G.); simelys.hernandez@polito.it (S.H.)
† These authors contributed equally to this work.
Abstract: Electrochemical CO
2
reduction is a promising carbon capture and utilisation technology.
Herein, a continuous flow gas diffusion electrode (GDE)-cell configuration has been studied to
convert CO
2
via electrochemical reduction under atmospheric conditions. To this purpose, Cu-based
electrocatalysts immobilised on a porous and conductive GDE have been tested. Many system
variables have been evaluated to find the most promising conditions able to lead to increased
production of CO
2
reduction liquid products, specifically: applied potentials, catalyst loading,
Nafion content, KHCO
3
electrolyte concentration, and the presence of metal oxides, like ZnO or/and
Al
2
O
3
. In particular, the CO productivity increased at the lowest Nafion content of 15%, leading to
syngas with an H
2
/CO ratio of ~1. Meanwhile, at the highest Nafion content (45%), C
2+
products
formation has been increased, and the CO selectivity has been decreased by 80%. The reported results
revealed that the liquid crossover through the GDE highly impacts CO
2
diffusion to the catalyst
active sites, thus reducing the CO
2
conversion efficiency. Through mathematical modelling, it has
been confirmed that the increase of the local pH, coupled to the electrode-wetting, promotes the
formation of bicarbonate species that deactivate the catalysts surface, hindering the mechanisms
for the C
2+
liquid products generation. These results want to shine the spotlight on kinetics and
transport limitations, shifting the focus from catalytic activity of materials to other involved factors.
Keywords: gas diffusion electrode; CO
2
reduction; electrocatalyst; copper; liquid fuels; mass trans-
port limitations
1. Introduction
Carbon dioxide (CO
2
) is an important trace gas in the Earth’s atmosphere, produced
by natural processes and human activities (e.g., fossil fuels use as an energy source).
With the aim of a transition towards the use of renewables energies, away from fossil
fuels, CO
2
can be regarded as a resource for beneficial processes. In such a context,
several routes can be followed to obtain added-value products, namely: stochiometric,
biochemical, photocatalytic, photoelectrochemical, electrochemical, and thermochemical.
The last two might be deemed the more encouraging approaches to obtaining added-value
products from CO
2
; however, improved reaction conditions and catalyst materials with
high activity and stability are still required [1]. This research work is focused on the
electrochemical route.
Electrocatalysis represents a promising method to increase the penetration of re-
newables into the fuels and chemicals industries, helping to close the carbon loop with
carbon-neutral electricity sources. Hence, among the advantages, it offers a way to handle
the growing world demand for resources, which greatly continues to depend on fossil fuels
Catalysts 2021, 11, 482. https://doi.org/10.3390/catal11040482 https://www.mdpi.com/journal/catalysts