Investigation of Practical Electro-catalysis using the Floating Electrode
Lead Research Organisation:
Imperial College London
Department Name: Chemistry
Abstract
The purpose of this project is to investigate the behaviour of electro-catalysts at the high current densities they need to operate at for industrial electro-catalysis applications. The main context of the project will be the cathode catalyst layer responsible for the oxygen reduction reaction (ORR) in PEM fuel cells. The ORR is the most difficult reaction in a PEM fuel cell and improvements to this reaction rate are the main route to lower cost membrane electrode assemblies (MEAs), because the currently required PGM loading on the MEA cathode is considered too high. Lower cost MEAs will enable wider penetration of fuel cells into existing and developing markets, such as automotive.
At present, only one electrochemical method is available that can probe electro-catalysis behaviour of gas diffusion electrodes outside of an MEA at high current density; this is the Floating Electrode (FE) method developed at Imperial College in Prof. Kucernak's group . The principle of the FE is shown in Figure 1: the electro-catalyst is simultaneously in contact with gaseous reactant, aqueous electrolyte and a good electronic conductor (sputtered gold). A key feature of the technique is its ability to bridge the gap between studying discrete electro-catalyst agglomerates and continuous catalyst layers of different PGM loading, whilst avoiding the complicating issues encountered using full-blown in-cell MEA testing. Whilst the feasibility and utility of this method has been shown by Chris Zalitis and bought in-house to JMTC, application of the FE has thrown up many new questions, for example:
1. Why does the mass activity of the ORR catalyst (Pt/C) apparently decrease significantly with increased electrode loading?
2. How limiting to the ORR is the proton conduction within the catalyst layer and within the electrolyte that the catalyst layer contacts (solid membrane or aqueous acid)?
3. Can it be definitively shown that Pt alloy catalysts are actually less active at high current densities than Pt-only catalysts, despite the converse being true at low current
densities?
Resolution of these questions will feed in to the FCR group understanding of the behaviour of MEAs and complimentary work will focus on applying the understanding to improved catalyst and catalyst layer design.
Once the fundamental questions above have been resolved, the project in its later stages can examine other gas-phase electro-catalyst systems. These will include the hydrogen evolution reaction, ubiquitous at the cathodes of industrial electrochemical processes such as electro-chlorination and central to the generation of hydrogen from renewable energy using PEM electrolysers. Further, the flexibility of electrochemical systems enables the use of intermittent renewable energy to synthesise valuable chemicals other than hydrogen, including ammonia and small chain hydrocarbons. The FE allows such high rate gas-consuming or gas evolving electrochemical reactions to be studied in a fundamental way under much more realistic conditions.
At present, only one electrochemical method is available that can probe electro-catalysis behaviour of gas diffusion electrodes outside of an MEA at high current density; this is the Floating Electrode (FE) method developed at Imperial College in Prof. Kucernak's group . The principle of the FE is shown in Figure 1: the electro-catalyst is simultaneously in contact with gaseous reactant, aqueous electrolyte and a good electronic conductor (sputtered gold). A key feature of the technique is its ability to bridge the gap between studying discrete electro-catalyst agglomerates and continuous catalyst layers of different PGM loading, whilst avoiding the complicating issues encountered using full-blown in-cell MEA testing. Whilst the feasibility and utility of this method has been shown by Chris Zalitis and bought in-house to JMTC, application of the FE has thrown up many new questions, for example:
1. Why does the mass activity of the ORR catalyst (Pt/C) apparently decrease significantly with increased electrode loading?
2. How limiting to the ORR is the proton conduction within the catalyst layer and within the electrolyte that the catalyst layer contacts (solid membrane or aqueous acid)?
3. Can it be definitively shown that Pt alloy catalysts are actually less active at high current densities than Pt-only catalysts, despite the converse being true at low current
densities?
Resolution of these questions will feed in to the FCR group understanding of the behaviour of MEAs and complimentary work will focus on applying the understanding to improved catalyst and catalyst layer design.
Once the fundamental questions above have been resolved, the project in its later stages can examine other gas-phase electro-catalyst systems. These will include the hydrogen evolution reaction, ubiquitous at the cathodes of industrial electrochemical processes such as electro-chlorination and central to the generation of hydrogen from renewable energy using PEM electrolysers. Further, the flexibility of electrochemical systems enables the use of intermittent renewable energy to synthesise valuable chemicals other than hydrogen, including ammonia and small chain hydrocarbons. The FE allows such high rate gas-consuming or gas evolving electrochemical reactions to be studied in a fundamental way under much more realistic conditions.
Publications

Jackson C
(2021)
Toward Understanding the Utilization of Oxygen Reduction Electrocatalysts under High Mass Transport Conditions and High Overpotentials
in ACS Catalysis

Lin X
(2020)
Electrocatalyst Performance at the Gas/Electrolyte Interface under High-Mass-Transport Conditions: Optimization of the "Floating Electrode" Method.
in ACS applied materials & interfaces

Wu J
(2020)
Controllable Heteroatom Doping Effects of CrxCo2-xP Nanoparticles: a Robust Electrocatalyst for Overall Water Splitting in Alkaline Solutions.
in ACS applied materials & interfaces
Studentship Projects
Project Reference | Relationship | Related To | Start | End | Student Name |
---|---|---|---|---|---|
EP/P51052X/1 | 30/09/2016 | 29/03/2022 | |||
2135758 | Studentship | EP/P51052X/1 | 14/10/2017 | 14/01/2022 | Xiaoqian Lin |
Description | We developed solid protocols for determining the ECSA and the true loading of the floating electrodes with Pt-based catalysts, utilizing CO stripping technique and ICP-MS. CO adsorption rather than hydrogen underpotential deposition (Hupd) should always be used to check the ECSA (electrochemically active surface area) of the Pt-based catalyst layer especially when the Pt loading is low, and hydrophobicity of the layer is key to facilitate high mass transport which agrees with the work on fuel cell electrodes. There are many different ways of making electrode hydrophobic. In the floating electrode system, we found that coating a very small amount of Teflon AF 2400 (a type of perfluoropolymer) on the electrode can increase its high current density (HCD) region performance by 100 times. We also compared three different perfluoropolymer materials with similar hydrophobicity and revealed that it is the gas permeability of perfluoropolymer (which acts as a barrier around the catalyst agglomerates) that mainly affects the maximum current density (power density) of both the hydrogen oxidation reaction (HOR) and the oxygen reduction reaction (ORR). With a Koutecký-Levich type analysis, we saw that when using Teflon AF 2400 which has the highest gas permeabilities, there is barely any mass transport limitation due to the perfluoropolymer. We provide insights into how Nafion ionomer content can affect the performance of the low-Pt loading catalyst layer. We compared different loadings of Nafion ionomers on the floating electrode and only saw a suppression on the HCD region of ORR, which disagrees with the results on rotating disk electrode (RDE) where a significant suppression can be seen at high low overpotential region (0.9 V vs. RHE) but is closer to the observations on fuel cell electrodes. Comparing our results for Nafion 900 and Nafion 1100 of the same structure but different total acid capacity, we suggested that this suppression is due to the sulphonate groups of Nafion ionomers. |
Exploitation Route | In this work, we have studied the possible factors that can significantly affect the performance of catalysts when assessed using the floating electrode technique to enable the standardization of this technique to measure high-performance electrocatalysts at the gas/liquid interface. Thanks to the resemblance of the floating electrode to the fuel cell electrode, we use this assessment to provide some insights into the low PGM content catalyst layers for fuel cells. |
Sectors | Energy Environment |
Description | Chemistry Department PG Symposium |
Form Of Engagement Activity | A talk or presentation |
Part Of Official Scheme? | No |
Geographic Reach | Local |
Primary Audience | Postgraduate students |
Results and Impact | A presentation was given to academics and other postgraduates from Imperial College London, and a 2nd prize was won for my presentation in the Energy Theme. It is believed that the Floating Electrode technique became more comprehensible and intriguing towards the audience. |
Year(s) Of Engagement Activity | 2019,2020 |
Description | Great Exhibition Road Festival 2019 |
Form Of Engagement Activity | Participation in an activity, workshop or similar |
Part Of Official Scheme? | No |
Geographic Reach | Local |
Primary Audience | Public/other audiences |
Results and Impact | We had fantastic opportunities for introducing our research to the public and we were thrilled to be flooded by all kinds of questions from people with great interests. The general public got more understanding of hydrogen fuel cell and how it is used in the automotive systems. |
Year(s) Of Engagement Activity | 2019 |
URL | https://www.greatexhibitionroadfestival.co.uk/ |