Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
  • H01M4/88—Processes of manufacture
  • H01M4/8803—Supports for the deposition of the catalytic active composition
  • H01M4/8807—Gas diffusion layers
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
  • H01M4/8605—Porous electrodes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
  • H01M4/88—Processes of manufacture
  • H01M4/8817—Treatment of supports before application of the catalytic active composition
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
  • H01M4/88—Processes of manufacture
  • H01M4/8825—Methods for deposition of the catalytic active composition
  • H01M4/8867—Vapour deposition
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M4/00—Electrodes
  • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
  • H01M4/90—Selection of catalytic material
  • H01M4/92—Metals of platinum group
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/02—Details
  • H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
  • H01M8/023—Porous and characterised by the material
  • H01M8/0234—Carbonaceous material
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/30—Hydrogen technology
  • Y02E60/50—Fuel cells
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
  • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

• the invention relates to a gas diffusion electrode (GDE), in particular to a gas diffusion electrode comprising an integral catalyst surface on a gas diffusion layer (GDL) and to processes for making the GDL.
• GDEs including the GDL, and fuel cells including the GDE are also protected.
• Fuel cells have potential for stationary and portable power applications in electric vehicles, buildings and other portable power generators.
• Low temperature fuel cells usually refer to polymer electrolyte membrane fuel cells (PEMFCs) and direct methanol fuel cells (DMFCs), employing solid protonic electrolyte, utilizing hydrogen or liquid fuels to deliver continuous power, have higher utilization efficiencies and intrinsically low polluting emissions comparing with conventional energy generators (e.g. Internal combustion engines).
• PEMFCs polymer electrolyte membrane fuel cells
• DMFCs direct methanol fuel cells
• solid protonic electrolyte utilizing hydrogen or liquid fuels to deliver continuous power
• conventional energy generators e.g. Internal combustion engines
• the commercial viability of low temperature fuel cells for power generation depends upon solving a number of manufacturing, cost, and durability problems, especially the hinder associated with the catalyst electrodes where the electrochemical reactions happen and the power generates.
• the conventional method for the fabrication of the catalyst electrode is usually a 3-step process.
• the catalyst e.g. platinum (Pt)
• Pt platinum
• the catalyst precursor is reduced to synthesize catalyst nanoparticles, and this usually occurs at a high temperature.
• support materials such as carbon black may be needed.
• surfactants are usually required. If this is done by polyol process, then organic solvents are often necessary.
• the catalyst nanoparticles are mixed with electrolyte ionomer and organic solvents to make a catalyst ink.
• the catalyst ink is coated onto gas diffusion layer (GDL) or electrolyte membrane surface to fabricate a catalyst electrode.
• GDL gas diffusion layer
• Fuel cells contain GDLs in order to allow gas to uniformly diffuse to the triple- phase boundary (TPB) in the catalyst layer, enabling the reaction gases (for instance hydrogen and oxygen) to contact with the catalyst and electrolyte thereby facilitating the fuel cell reaction.
• the most commonly used GDL materials are Teflon treated carbon paper or carbon cloth covered with a porous layer that contains carbon black spheres and Teflon. These materials are usually hydrophobic in order to remove water from the fuel cell and so prevent the fuel cell from flooding.
• the highly hydrophobic feature of the GDL surface makes it difficult to use the surface as a direct support for depositing electrocatalysts in aqueous systems, which finally results in an non-uniform Platinum nanowire distribution on the GDL surface as mentioned above.
• a GDL which can provide good fuel cell performance, and preferably an integral catalyst surface.
• the invention is intended to overcome or ameliorate at least some aspects of this problem.
• a GDE comprising a GDL with a surface to which platinum nanowires have been applied; wherein the surface is at least partially hydrophobic or hydrophilic, forming a weakly hydrophobic surface or hydrophilic regions on the surface of the GDL.
• the platinum nanowires or nanowire arrays form a catalyst layer on the GDL surface, the layer (or coating) being total, effectively total or partial on the GDL surface.
• total coverage would be 100%; effectively total in the range 80 - 99.9% or 95 - 99.5% of the surface area covered or coated; and partial being in the range 30 - 95% of the surface, often 50 - 95% or 70 - 80% of the surface being coated with the platinum nanowire arrays.
• hydrophilic surface is intended to mean a surface with a water contact angle of less than 90° (perhaps in the range 1-90°, 15-85°, or 30-60°) and the term “hydrophobic surface” is intended to mean a surface with a water contact angle of greater than 90° (perhaps in the range 90-179°, 95-150°, or 105-130°).
• weakly hydrophobic surface is intended to mean a surface with a water contact angle between 90- 130° (perhaps in the range 90-120° or 90-105°); the term “highly hydrophobic surface” means a surface with a water contact angle in the range of 130-150°; and the term “superhydrophobic surface” means a surface with a water contact angle greater than 150° (perhaps in the range 150-175° or 155-165°).
• highly hydrophilic surface means a surface with a water contact angle in the range of 30-60°; and the term “weakly hydrophilic surface” means a surface with a water contact angle between 60-90°, often 75-90°.
• reference to a weakly hydrophobic/hydrophilic surface, or region is intended to include surfaces/regions which are weakly hydrophobic, hydrophilic and combinations thereof.
• this surface may be entirely or substantially entirely hydrophilic/weakly hydrophobic (for instance, wherein the surface has a surface area which is greater than 95% hydrophilic/weakly hydrophobic, greater than 97%, 98%, or 99% hydrophilic/weakly hydrophobic. In some cases, the surface may be greater than 99.5% hydrophilic/weakly hydrophobic. Often the surface will be 100% hydrophilic/weakly hydrophobic, or slightly less than 100% hydrophilic/weakly hydrophobic, such as 99.9% or less, 99.8% or less or 99.5% or less).
• hydrophilic/weakly hydrophobic is less than 95% hydrophilic/weakly hydrophobic, we will refer to it herein as being a surface including hydrophilic/weakly hydrophobic regions on the surface.
• the hydrophilic/weakly hydrophobic regions will often form in the range 50 - 95% of the surface, often 60 - 85%, or 70 - 80% of the surface.
• the surface itself will often have a surface area which is in the range 50 - 100% hydrophilic/weakly hydrophobic, or 60 - 90%, or 70 - 80% hydrophilic/weakly hydrophobic.
• the platinum nanowires substantially cover the hydrophilic/weakly hydrophobic surface or hydrophilic/weakly hydrophobic regions on the surface of the GDL, as this is where the reaction solution can reach and form nucleus of catalyst metal and finally grow to single-crystal nanowire.
• the platinum nanowires will cover in the range 50 - 99% of the surface area of hydrophilic surface or hydrophilic regions on the surface, often 85 - 95%, or 90 - 95% of the hydrophilic/weakly hydrophobic surface or hydrophilic/weakly hydrophobic regions on the surface.
• the GDL substrate may be selected from any of the many substrates are usually used in fuel cells, although often the substrate will be a substrate used in low temperature fuel cells such as carbon cloth, carbon paper or carbon paper with a porous layer.
• the carbon paper and carbon cloth may be woven or non-woven and may be coated, for instance with TeflonTM.
• the substrate/GDL may have a porous layer. Where present the porous layer may be a layer between the catalyst layer and GDL support in the GDE. The presence of a porous layer allows uniform diffusion of the gaseous reaction media to the catalyst, whilst supporting the catalyst layer where necessary.
• the platinum nanowires are typically of length in the range 50 - 500 nm, and/or of diameter in the range 1 - 10 nm. This allows the preparation of a remarkably thin catalyst layer, of thickness less than 1 ⁇ .
• the thickness of the catalyst layer may be in the range 50 nm - ⁇ , often 100 - 500 nm, or 300 - 400 nm. Often the length of the nanowires will be in the range 100 - 400 nm, or 200 - 300 nm.
• the diameter of the nanowires will be in the range 1 - 10 nm, often 2 - 6 nm, allowing dense packing of nanowires across the hydrophilic/weakly hydrophobic surface or hydrophilic/weakly hydrophobic regions on the surface.
• Such a thin catalyst layer can be achieved as the catalyst layer is typically constructed from a monolayer of platinum nanowire arrays.
• This novel structure significantly reduces the mass transfer resistance relative to conventional GDEs that usually have a catalyst layer with a thickness about 10 ⁇ .
• the application of platinum nanowires to the hydrophilic/weakly hydrophobic surface to form the GDE provides a GDE with a much improved catalytic performance towards oxygen reduction reaction (ORR) in low temperature fuel cells, e.g. PEMFCs and DMFCs, than has previously been observed.
• ORR oxygen reduction reaction
• the physical dimensions of the GDL/GDE are not particularly limited, the simplicity of the GDE ensures that it is easy to prepare regardless of the product size, providing flexibility not previously available.
• the GDE may be of thickness similar to known GDE's, for instance in the range 10 - 500 ⁇ , with the resulting GDE being of active area in the range 1 mm 2 - 1 m 2 as necessary for the application. Plasma treatment is possible across this wide range of sizes.
• the platinum nanowires act as catalysts, and can do so effectively as the presence of the hydrophilic/weakly hydrophobic surface or hydrophilic/weakly hydrophobic regions on the surface promote a uniform distribution of nanowires in catalyst layer, resulting in good, reliable catalytic activity of the GDE.
• a membrane electrode assembly (MEA) for fuel cell comprising the GDE of the first aspect of the invention.
• the fuel cell will be a low temperature fuel cell such as a DMFC or a PEMFC.
• the incorporation of the GDE of the invention into such fuel cells reduces production costs and improves the reliability of the fuel cell as there are fewer components present to foul.
• a process for making a GDE comprising the steps of:
• Treatment of the surface with plasma converts highly/superhydrophobic end groups to weakly hydrophobic or even hydrophilic end groups, creating more nucleation sites and enabling the application of the platinum nanowires.
• the plasma treatment enhances the wettability of the GDL, allowing for the application of the platinum nanowires to the surface in sufficient quantities, and with a sufficiently even distribution, to give a high catalytic activity to a GDE.
• the GDL, and hence also the GDE, are very easy to construct, as the plasma techniques and platinum nanowire deposition process used are very simple, and hence easily to scale up.
• the GDE can be prepared using a single step from the plasma treated GDL, which can be conducted at room temperature.
• known processes for preparing GDEs require (in addition to the provision of a GDL), the steps of making a catalyst ink and coating to fabricate the catalyst layer. These steps are not needed with the products of the invention, removing two of the three production steps for GDEs.
• the process of the invention is a green and clean chemical process because there is no waste, and because (despite the use of nanowires in the GDE construction), the whole procedure does not at any point generate free (potentially toxic) nanoparticles.
• the platinum nanowires are applied to the plasma treated surface by being grown onto the plasma treated surface.
• a wide variety of techniques may be used, as would be known to the person skilled in the art, although it will often be the case that the technique used will be selected from physical vapour deposition, chemical vapour deposition, chemical reduction deposition, or combinations thereof.
• the platinum-containing precursor will often be reduced on the plasma treated surface of the GDL.
• the platinum-containing precursor need only be such that it can be reduced to platinum under relatively mild conditions, without inhibiting the nanowire growth process or fouling the GDL.
• the platinum- containing precursor is selected from chloroplatinic acid (hexa)hydrate, platinic acid, sodium platinic chloride, potassium hexachloroplatinate, and combinations thereof.
• Weak reducing agents are often used, to ensure that the GDL is not damaged, and that the nanowire growth process not prevented in any way.
• the reducing agent will be selected from hydrogen, formic acid, ascorbic acid, citric acid and combinations thereof.
• platinum nanowire growth can be achieved at room temperature, without using organic solvents, template, or inducing growth catalysts, which are usually necessary in fabricating conventional catalyst electrodes in fuel cells.
• vapour deposition techniques may be used, these include physical and chemical vapour deposition and would be well known to the skilled reader.
• Such techniques can be advantageous in that the nanowire growth is easy to control and so an evenly distributed catalyst layer will be produced; however, as such techniques are more complex than chemical reduction methods, often reduction techniques will be used in the subject invention.
• the plasma treatment can be completed in a conventional plasma furnace, and active-screen furnaces are often used.
• the plasma gas may be hydrogen carried in an inert gas, such as argon or nitrogen, of which often nitrogen will be used.
• an inert gas such as argon or nitrogen
• the ratio will be 1: 1 hydrogen:nitrogen or greater.
• the ratio will be in the range 2: 1 - 5: 1, often around 3: 1 hydrogen: nitrogen.
• plasma treatment will generally be at a relatively low temperature, for instance in the range 50 - 250°C, often 75 - 200°C, often around 100°C, so in the range 80 - 120 °C or 90 - 110°C. This is advantageous as only minimal energy is consumed during the plasma treatment process.
• the duration of treatment can be short, for instance less than 2 hours, often less than 1 hour, less 30 minutes, often around 15 minutes. A range of 5 - 120 minutes would be typical, with upper limits as above.
• Figures la and lb show SEM images of GDEs with in-situ grown single crystal platinum nanowire arrays on un-treated (a) and plasma treated (b) SIGRACET ® GDL 35BC carbon paper (Thickness: 325 + 25 microns; Area Weight: 110 + 10 g/m 2 ; Air permeability: 1.50 + 1.00 cm 3 /(cm 2 - s); Electrical resistivity (TP): ⁇ 15 milliohms cm 2 );
• Figures 2a and 2b show a comparison of the water contact angles for SIGRACET ® GDL 35BC before (a) and after (b) plasma treatment;
• Figure 3 shows I-V and P-V of single DMFCs with a range of cathodes, including Johnson-Matthey DMFC cathode (Alfa Catalog Number: 045375; Non-woven carbon fibres: 60 wt%; Catalyst: 25 wt%; Carbon Black: 5 wt%; PTFE: 5 wt%; PFSA ionomer: 5 wt%) ( ⁇ ), a GDE with platinum nanowire array on un-treated carbon paper ( ⁇ ), and a GDE with platinum nanowire array on plasma treated carbon paper (A).
• the platinum loadings are 4 mg cm - " 2 (Johnson-Matthey), 4 mg cm - " 2 (platinum nanowire GDEs on untreated carbon paper) and 2 mg cm " (platinum nanowire GDEs on plasma treated carbon paper);
• Figures 4a and 4b show a comparison of the water wetting angle for E-TEK ® GDL 1200-W (Thickness: 275 microns; Basis weight: 200 g/m 2 ; Air permeability: >8 cm 3 /(cm 2 - s); Electrical resistivity (TP): 410 milliohms-cm) before (a) and after (b) plasma treatment; and [0041]
• Figure 5 shows I-V and P-V of single PEMFCs with cathodes of commercial E- TEK ® GDE LT-120EW (Thickness: 310 microns; Basis weight: 180 g/m 2 ; Air permeability: 40 cm 3 /(cm 2 - s); Electrical resistivity (TP): 685 milliohms-cm) ( ⁇ ), GDEs with platinum nanowire array on un-treated carbon cloth ( ⁇ ), and GDEs with platinum nanowire array on plasma treated carbon cloth (A).
• the platinum loadings are 0.5 mg
• Example 1 DMFC cathode with single crystal platinum nanowire arrays grown on SIGRACET ® GDL 35BC
• GDL 35BC GDL 35BC carbon paper
• GDL 35BC was surface treated in an active-screen plasma furnace at 100°C for 15 minutes in a gas mixture of 75% H 2 /25% N 2 .
• Figures 2a and 2b show the water wetting angle for SIGRACET ® GDL 35BC before and after plasma treatment.
• Figure 2b where the GDL has been plasma treated, the surface has a reduced wetting angle compared to Figure 2a.
• MEA Membrane Electrode Assembly
• the platinum nanowire GDEs with treated or un-treated GDL were assembled as cathodes with NAFION ® NR-117 membranes (EW: 1100; Thickness: 183 microns; Basis weight: 360 g/m 2 ; specific gravity: 1.97 g/cm 3 ) to fabricate MEAs.
• NAFION ® NR-117 membranes EW: 1100; Thickness: 183 microns; Basis weight: 360 g/m 2 ; specific gravity: 1.97 g/cm 3
• the comparative MEA was simultaneously fabricated with a NAFION ® NR-117 membrane and commercial Johnson Matthey DMFC cathode (4 mg Pt cm “2 ) and anode used as both electrodes. Teflon ® film with a thickness of 254 ⁇ was used as gasket material in the DMFC hardware.
• the MEA was sandwiched between two stainless steel flow field plates to form a single cell with an active electrode area of 5 cm 2 .
• the single cell test was performed at 75°C using an automatic fuel cell test system (EZstat-Pro, 1A, NuVant Systems Inc., USA).
• the anode was fed with 1 molL -1 methanol at a flow rate of 1 mLmin -1 without back pressure.
• the cathode was fed with non-humidified air at a flow rate of 100 standard cubic centimeters per minute (seem) without back pressure.
• the cell was conditioned with nanopure water at the anode and air at the cathode at 75°C. After conditioning, nanopure water was replaced with aqueous methanol for 24h in galvanostatic mode at 10 mA cm " . Then the cell voltage was looped between 0.2 and 0.7 V at 5 mVs -1 for 5 cycles, and the fifth cycle was recorded.
• Example 2 PEMFC cathode with single crystal platinum nanowire arrays grown on E-TEK ® GDL 1200-W
• a 4x4 cm 2 piece of E-TEK ® GDL 1200-W carbon cloth was used as a GDL substrate to grow platinum nanowires. All other details are the same as in Example 1, except the amounts of chemicals used, which were as follows. To grow 0.4 mg cm " platinum nanowires on GDLs, 16.99 mg H 2 PtCl 6 - 6H 2 0 (6.4 mg Pt, 0.4 mg cm “2 on GDL) was added into 10.6 mL aqueous solution containing 0.53 mL formic acid.
• the MEAs were tested in a 16 cm -PEMFC single cell hardware at a temperature of 70°C, using pure H 2 and air gases at 50% relative humidity (RH) and gas flows in the range of 120 and 300 mLmin "1 with stoichiometries of 1.5(H 2 )/2.0(Air) respectively.
• the back pressure of the humidified H 2 and air was 0.15 MPa. Measurements were controlled and recorded by a Bio-logic FCT-50S PEMFC test station (PaxiTech).
• the MEA was conditioned by break-in at 0.6 V for 12 hours, and thereafter the polarization curves were recorded at a scan rate of 1 mV s "1 .
• the polarization and power density curves for three MEAs are shown in Figure 5. As can be seen, the plasma treated platinum nanowire array outperforms both current commercial systems (E- TEK ® ), and the untreated systems.
• GDL' s, GDE's, fuel cells and processes of the invention are capable of being incorporated in the form of a variety of embodiments, only a few of which have been illustrated and described above.

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• 2012
  • 2012-02-28 GB GBGB1203409.6A patent/GB201203409D0/en not_active Ceased
• 2013
  • 2013-02-19 WO PCT/GB2013/050393 patent/WO2013128163A1/fr not_active Ceased

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