EP3881384A1 - Procédé de fabrication à contrôle de taille de particules - Google Patents

Procédé de fabrication à contrôle de taille de particules

Info

Publication number
EP3881384A1
EP3881384A1 EP19886007.4A EP19886007A EP3881384A1 EP 3881384 A1 EP3881384 A1 EP 3881384A1 EP 19886007 A EP19886007 A EP 19886007A EP 3881384 A1 EP3881384 A1 EP 3881384A1
Authority
EP
European Patent Office
Prior art keywords
fuel cell
anode
electrolyte
cathode
particles
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
EP19886007.4A
Other languages
German (de)
English (en)
Other versions
EP3881384A4 (fr
Inventor
David R. Hall
Matthew Dawson
Nicholas FARANDOS
Jin Dawson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Utility Global Inc
Original Assignee
Utility Global Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US16/674,580 external-priority patent/US20200176803A1/en
Application filed by Utility Global Inc filed Critical Utility Global Inc
Priority claimed from PCT/US2019/060838 external-priority patent/WO2020102140A1/fr
Publication of EP3881384A1 publication Critical patent/EP3881384A1/fr
Publication of EP3881384A4 publication Critical patent/EP3881384A4/fr
Pending legal-status Critical Current

Links

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
    • H01M4/8825—Methods for deposition of the catalytic active composition
    • H01M4/8828—Coating with slurry or ink
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B18/00—Layered products essentially comprising ceramics, e.g. refractory products
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    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/016—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on manganites
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    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
    • C04B35/62605—Treating the starting powders individually or as mixtures
    • C04B35/62625—Wet mixtures
    • C04B35/6264—Mixing media, e.g. organic solvents
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    • H01M4/8878—Treatment steps after deposition of the catalytic active composition or after shaping of the electrode being free-standing body
    • H—ELECTRICITY
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    • C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/26—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on ferrites
    • C04B35/2641—Compositions containing one or more ferrites of the group comprising rare earth metals and one or more ferrites of the group comprising alkali metals, alkaline earth metals or lead
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/42—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on chromites
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/45—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on copper oxide or solid solutions thereof with other oxides
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/48—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on zirconium or hafnium oxides, zirconates, zircon or hafnates
    • C04B35/486—Fine ceramics
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/50—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on rare-earth compounds
    • 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

Definitions

  • This invention generally relates to methods of manufacturing. More specifically, this invention relates to manufacturing methods with particle size control.
  • a fuel cell is an electrochemical apparatus or electrochemical reactor that converts the chemical energy from a fuel into electricity through an electrochemical reaction.
  • the heat generated by a fuel cell is also usable.
  • fuel cells There are many types of fuel cells.
  • PEMFCs proton-exchange membrane fuel cells
  • MEA membrane electrode assemblies
  • An ink of catalyst, carbon, and electrode are sprayed or painted onto the solid electrolyte and carbon paper is hot pressed on either side to protect the inside of the cell and also act as electrodes.
  • the most important part of the cell is the triple phase boundary where the electrolyte, catalyst, and reactants mix and thus where the cell reactions actually occur.
  • the membrane must not be electrically conductive so that the half reactions do not mix.
  • PEMFC is a good candidate for vehicle and other mobile applications of all sizes (e.g., mobile phones) because it is compact.
  • water management is crucial to performance: too much water will flood the membrane, too little will dry it; in both cases, power output will drop.
  • Water management is a difficult problem in PEM fuel cell systems, mainly because water in the membrane is attracted toward the cathode of the cell through polarization.
  • the platinum catalyst on the membrane is easily poisoned by carbon monoxide (CO level needs to be no more than one part per million).
  • CO level carbon monoxide
  • the membrane is also sensitive to things like metal ions, which can be introduced by corrosion of metallic bipolar plates, or metallic components in the fuel cell system, or from contaminants in the fuel and/or oxidant.
  • Solid oxide fuel cells are a different class of fuel cells that use a solid oxide material as the electrolyte.
  • SOFCs use a solid oxide electrolyte to conduct negative oxygen ions from the cathode to the anode.
  • the electrochemical oxidation of the oxygen ions with fuel e.g., hydrogen, carbon monoxide
  • Some SOFCs use proton conducting electrolytes (PC-SOFCs), which transport protons instead of oxygen ions through the electrolyte.
  • PC-SOFCs proton conducting electrolytes
  • SOFCs using oxygen ion conducting electrolytes have higher operating temperatures than PC-SOFCs.
  • SOFCs do not typically require expensive platinum catalyst material, which is typically necessary for lower temperature fuel cells such as proton- exchange membrane fuel cells (PEMFCs), and are not vulnerable to carbon monoxide catalyst poisoning.
  • Solid oxide fuel cells have a wide variety of applications, such as auxiliary power units for homes and vehicles as well as stationary power generation units for data centers.
  • SOFCs comprise interconnects, which are placed between each individual cell so that the cells are connected in series and that the electricity generated by each cell is combined.
  • One category of SOFC is segmented-in-series (SIS) type SOFC, in which electrical current flow is parallel to the electrolyte in the lateral direction. Contrary to the SIS type SOFC, a different category of SOFC has electrical current flow perpendicular to the electrolyte in the lateral direction.
  • a method of making an object comprising mixing particles with a liquid to form a dispersion; depositing the dispersion on a substrate to form a layer; and treating the layer to cause at least a portion of the particles to sinter, wherein the particles have a size distribution that has at least one of the following characteristics: (a) said size distribution comprises DIO and D90, wherein 10% of the particles have a diameter no greater than D10 and 90% of the particles have a diameter no greater than D90, wherein D90/D10 is in the range of from 1.5 to 100; or (b) said size distribution is bimodal such that the average particle size in the first mode is at least 5 times the average particle size in the second mode; or (c) said size distribution comprises D50, wherein 50% of the particles have a diameter no greater than D50, wherein D50 is no greater than 100 nm.
  • D50 is no greater than 50 nm, or no greater than 30 nm, or no greater than 20 nm, or no greater than 10 nm, or no greater than 5 nm.
  • the average particle size in the first mode is at least 10 times or 15 times or 20 times the average particle size in the second mode.
  • DIO is in the range of from 5 nm to 50 nm or from 5 nm to 100 nm or from 5 nm to 200 nm; or wherein D90 is in the range of from 50 nm to 500 nm or from 50 nm to 1000 nm.
  • D90/D10 is in the range of from 2 to 100 or from 4 to 100 or from 2 to 20 or from 2 to 10 or from 4 to 20 or from 4 to 10.
  • the particles have a diameter in the range of from 1 nm to 1000 nm, wherein D10 is in the range of from 1 nm to 10 nm and D90 is in the range of from 50 nm to 500 nm.
  • the layer has a thickness of no greater than 1 mm or no greater than 500 microns or no greater than 300 microns or no greater than 100 microns or no greater than 50 microns.
  • said object comprises a catalyst, a catalyst support, a catalyst composite, an anode, a cathode, an electrolyte, an electrode, an interconnect, a barrier, a seal, a fuel cell, an electrochemical gas producer, an electrolyser, an electrochemical compressor, a reactor, a heat exchanger, a vessel, or combinations thereof.
  • depositing comprises material jetting, binder jetting, inkjet printing, aerosol jetting, or aerosol jet printing, vat photopolymerization, powder bed fusion, material extrusion, directed energy deposition, sheet lamination, ultrasonic inkjet printing, or combinations thereof.
  • said liquid comprises water and at least one organic solvent miscible with water, or wherein said liquid comprises water, a surfactant, a dispersant, and no polymeric binder, or wherein said liquid comprises one or more organic solvents and no water.
  • the organic solvent is selected from the group consisting of methanol, ethanol, butanol, isopropyl alcohol, terpineol, diethyl ether, 1,2-dimethoxyethane (DME or ethylene glycol dimethyl ether), 1-propanol (n-propanol or n-propyl alcohol), butyl alcohol, ethylene glycol, propylene glycol, dipropylene glycol, and combinations thereof.
  • the particles comprise Cu, CuO, CU2O, Ag, Ag 2 0, Au, AU2O, AU2O3, titanium, Yttria-stabilized zirconia (YSZ), 8YSZ (8mol% YSZ powder), Yttirum, Zirconium, gadolinia-doped ceria (GDC or CGO), Samaria-doped ceria (SDC), Scandia-stabilized zirconia (SSZ), Lanthanum strontium manganite (LSM), Lanthanum Strontium Cobalt Ferrite (LSCF), Lanthanum Strontium Cobaltite (LSC), Lanthanum Strontium Gallium Magnesium Oxide (LSGM), Nickel (Ni), NiO, NiO-YSZ, Cu-CGO, cerium, crofer, steel, lanthanum chromite, doped lanthanum chromite, ferritic steel, stainless steel, or combinations thereof.
  • YSZ Yttria-
  • the method comprises drying the dispersion after depositing.
  • drying comprises heating the dispersion before deposition, heating the substrate that is contact with the dispersion, or combination thereof.
  • drying takes place for a period in the range of no greater than 5 minutes, or no greater than 3 minutes, or no greater than 1 minute, or from 1 s to 30 s, or from 3 s to 10 s.
  • the dispersion is deposited at a temperature in the range of from 40°C to 100°C or from 50°C to 90°C or from 60°C to 80°C or about 70°C.
  • treating comprises the use of electromagnetic radiation (EMR), or a furnace, or plasma, or hot fluid, or a heating element, or combinations thereof.
  • EMR electromagnetic radiation
  • the electromagnetic radiation comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam, microwave.
  • the electromagnetic radiation is provided by a xenon lamp.
  • the particle size distribution is determined by dynamic light scattering or transmission electron microscopy.
  • Figure 1 illustrates a fuel cell comprising an anode, an electrolyte, and a cathode, according to an embodiment of this disclosure.
  • Figure 2 illustrates a fuel cell comprising an anode, an electrolyte, at least one barrier layer, and a cathode, according to an embodiment of this disclosure.
  • Figure 3 illustrates a fuel cell comprising an anode, a catalyst, an electrolyte, at least one barrier layer, and a cathode, according to an embodiment of this disclosure.
  • Figure 4 illustrates a fuel cell comprising an anode, a catalyst, an electrolyte, at least one barrier layer, a cathode, and an interconnect, according to an embodiment of this disclosure.
  • Figure 5 illustrates a fuel cell stack, according to an embodiment of this disclosure.
  • FIG. 6 illustrates a method and system of integrated deposition and heating using electromagnetic radiation (EMR), according to an embodiment of this disclosure.
  • EMR electromagnetic radiation
  • Figure 7 illustrates SRTs of a first composition and a second composition as a function of temperature, according to an embodiment of this disclosure.
  • Figure 8 illustrates a process flow for forming and heating at least a portion of a fuel cell, according to an embodiment of this disclosure.
  • Figure 9 illustrates maximum height profile roughness, according to an embodiment of this disclosure.
  • FIG. 10A illustrates an electrochemical (EC) gas producer comprising a first electrode, an electrolyte, and a second electrode, wherein the first electrode receives methane and water or methane and carbon dioxide and the second electrode receives water, according to an embodiment of this disclosure.
  • EC electrochemical
  • Figure 10B illustrates an EC gas producer comprising a first electrode, an electrolyte, and a second electrode, wherein the first electrode receives methane and water or methane and carbon dioxide and the second electrode receives nothing, according to an embodiment of this disclosure.
  • Figure IOC illustrates an electrochemical compressor comprising anodes, electrolytes, cathodes, porous bipolar plates, a fluid distributor on one end, and a fluid collector on the other end, according to an embodiment of this disclosure.
  • Figure 11A illustrates a perspective view of a fuel cell cartridge (FCC), according to an embodiment of this disclosure.
  • Figure 11B illustrates cross-sectional views of a fuel cell cartridge (FCC), according to an embodiment of this disclosure.
  • FIG. 11C illustrates top view and bottom view of a fuel cell cartridge (FCC), according to an embodiment of this disclosure.
  • Figure 12 is a scanning electron microscopy image (side view) illustrating an electrolyte (YSZ) printed and sintered on an electrode (NiO-YSZ), according to an embodiment of this disclosure.
  • compositions and materials are used interchangeably unless otherwise specified. Each composition/material may have multiple elements, phases, and components. Heating as used herein refers to actively adding energy to the compositions or materials.
  • in situ in this disclosure refers to the treatment (e.g., heating) process being performed either at the same location or in the same device of the forming process of the compositions or materials.
  • the deposition process and the heating process are performed in the same device and at the same location, in other words, without changing the device and without changing the location within the device.
  • the deposition process and the heating process are performed in the same device at different locations, which is also considered in situ.
  • particle size is used to describe an important property of the particles used in the disclosed methods.
  • Particle size can be measured by various means known in the art, some of which are based on light (such as dynamic light scattering), others on ultrasound, or electric field, or gravity, or centrifugation.
  • the size is an indirect measure, obtained by a model that transforms, in a mathematical way, the real particle shape into a simple and standardized shape, like a sphere, where the size parameter, such as the diameter of sphere, makes sense.
  • a major face of an object is the face of the object that has a surface area larger than the average surface area of the object, wherein the average surface area of the object is the total surface area of the object divided by the number of faces of the object.
  • a major face refers to a face of an item or object that has a larger surface area than a minor face.
  • a major face is the face or surface in the lateral direction.
  • strain rate tensor or "SRT” is meant to refer to the rate of change of the strain of a material in the vicinity of a certain point and at a certain time. It can be defined as the derivative of the strain tensor with respect to time. When SRTs or difference of SRTs are compared in this disclosure, it is the magnitude that is being used.
  • lateral refers to the direction that is perpendicular to the stacking direction of the layers in a non-SIS type fuel cell.
  • lateral direction refers to the direction that is perpendicular to the stacking direction of the layers in a fuel cell or the stacking direction of the slices to form an object during deposition.
  • Lateral also refers to the direction that is the spread of deposition process.
  • Syngas i.e., synthesis gas in this disclosure refers to a mixture consisting primarily of hydrogen, carbon monoxide, and carbon dioxide.
  • absorbance is a measure of the capacity of a substance to absorb electromagnetic radiation (EMR) of a wavelength.
  • EMR electromagnetic radiation
  • An impermeable layer or interconnect as used herein refers to a layer or interconnect that is impermeable to fluid flow.
  • an impermeable layer has a permeability of less than 1 micro darcy, or less than 1 nano darcy.
  • an interconnect having no fluid dispersing element refers to interconnect having no elements (e.g., channels) to disperse a fluid. Such an interconnect may have inlets and outlets for materials or fluids to pass through.
  • microchannels are used interchangeably with microfluidic channels or microfluidic flow channels.
  • sintering refers to a process to form a solid mass of material by heat or pressure or combination thereof without melting the material to the extent of
  • Tsinter refers to the temperature at which this phenomenon begins to take place.
  • the term "absorber particles” refer to particles that have greater absorption of energy than ceramic particles for a given electromagnetic radiation (EMR) spectrum.
  • EMR electromagnetic radiation
  • the ceramic particles are CGO
  • absorber particles are copper particles or copper oxide particles or LSCF particles.
  • the ceramic particles are YSZ, absorber particles are copper particles or copper oxide particles or LSCF particles or Cu- CGO particles.
  • the absorber particles having no appreciable flow if they are melted means that the layer of the absorber particles has a change in one dimension (length, width, height) by no more than 10% or by no more than 5% or by no more than 1% (which most preferably is 0%).
  • an insulator such as that used in the insulator layer refers to a substance that does not readily allow the passage of heat.
  • an insulator has a thermal conductivity of no greater than 1 W/(m K).
  • the insulator has a thermal conductivity of no greater than 0.1 W/(m K).
  • SOFCs solid oxide fuel cells
  • electrochemical device examples include electrochemical (EC) gas producer, electrochemical (EC) compressor, and batteries.
  • Catalysts include Fischer Tropsch (FT) catalyst, reformer catalyst.
  • Reactor/vessel includes FT reactor, heat exchanger.
  • a method comprising depositing a composition on a substrate slice by slice to form an object; heating in situ the object using electromagnetic radiation (EMR); wherein said composition comprises a first material and a second material, wherein the second material has a higher absorbance of the radiation than the first material.
  • EMR electromagnetic radiation
  • the EMR has a peak wavelength ranging from 10 to 1500 nm and the EMR has a minimum energy density of 0.1 Joule/cm 2 , wherein the peak wavelength is on the basis of relative irradiance with respect to wavelength.
  • the EMR comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam.
  • Figure 6 illustrates an object on a substrate formed by deposition nozzles and EMR for heating in situ, according to an embodiment of this disclosure.
  • the first material comprises Yttria-stabilized zirconia (YSZ), 8YSZ (8mol% YSZ powder), Yttirum,
  • GDC or CGO gadolinia-doped ceria
  • SDC Samaria-doped ceria
  • SSZ Scandia-stabilized zirconia
  • LSM Lanthanum strontium manganite
  • LSCF Lanthanum Strontium Cobalt Ferrite
  • LSC Lanthanum Strontium Cobaltite
  • LSGM Lanthanum Strontium Gallium Magnesium Oxide
  • Nickel, NiO, NiO-YSZ Cu-CGO, CU2O, CuO, Cerium, copper, silver, crofer, steel, lanthanum chromite, doped lanthanum chromite, ferritic steel, stainless steel, or combinations thereof.
  • the first material comprises YSZ, SSZ, CGO, SDC, NiO-YSZ, LSM-YSZ, CGO-LSCF, doped lanthanum chromite, stainless steel, or combinations thereof.
  • the second material comprises carbon, nickel oxide, nickel, silver, copper, CGO, SDC, NiO-YSZ, NiO-SSZ, LSCF, LSM, doped lanthanum chromite ferritic steels, or combinations thereof.
  • said object comprises a catalyst, a catalyst support, a catalyst composite, an anode, a cathode, an electrolyte, an electrode, an interconnect, a seal, a fuel cell, an electrochemical gas producer, an electrolyser, an electrochemical compressor, a reactor, a heat exchanger, a vessel, or combinations thereof.
  • the second material is a deposited in the same slice as the first material.
  • the second material is a deposited in a slice adjacent another slice that contains the first material.
  • said heating removes at least a portion of the second material.
  • said removing leaves minimal residue of the portion of the second material.
  • this step leaves minimal residue of the portion of the second material, which is to say that there is no significant residue that would interfere with the subsequent steps in the process or the operation of the device being constructed. More preferably, this leaves no measurable reside of the portion of the second material.
  • the second material adds thermal energy to the first material during heating.
  • the second material has a radiation absorbance that is at least 5 times that of the first material; or the second material has a radiation absorbance that is at least 10 times that of the first material; the second material has a radiation absorbance that is at least 50 times that of the first material; the second material has a radiation absorbance that is at least 100 times that of the first material.
  • the second material has a peak absorbance wavelength no less than 200 nm, or 250 nm, or 300 nm, or 400 nm, or 500 nm.
  • the first material has a peak absorbance wavelength no greater than 700 nm, or 600 nm, or 500 nm, or 400 nm, or 300 nm. In an embodiment, the EMR has a peak wavelength no less than 200 nm, or 250 nm, or 300 nm, or 400 nm, or 500 nm.
  • the second material comprises carbon, nickel oxide, nickel, silver, copper, CGO, NiO-YSZ, LSCF, LSM, ferritic steels, or combinations thereof. In some cases, the ferritic steel is Crofer 22 APU.
  • the first material comprises YSZ, CGO, NiO-YSZ, or LSM-YSZ.
  • the second material comprises LSCF, LSM, carbon, nickel oxide, nickel, silver, copper, or steel. In an embodiment, carbon comprises graphite, graphene, carbon nanoparticles, nano diamonds, or combinations thereof.
  • said depositing comprises material jetting, binder jetting, inkjet printing, aerosol jetting, or aerosol jet printing, vat photopolymerization, powder bed fusion, material extrusion, directed energy deposition, sheet lamination, ultrasonic inkjet printing, or combinations thereof.
  • the method comprises controlling distance from the EMR to the substrate, EMR energy density, EMR spectrum, EMR voltage, EMR exposure duration, EMR exposure area, EMR exposure volume, EMR burst frequency, EMR exposure repetition number, or combinations thereof.
  • the object does not change location between depositing and heating.
  • the EMR has a power output of no less than 1 W, or 10 W, or 100 W, or 1000 W.
  • a system comprising at least one deposition nozzle, an electromagnetic radiation (EMR) source, and a deposition receiver, wherein the deposition receiver is configured to receive EMR exposure and deposition at the same location.
  • the receiver is configured such that it receives deposition for a first time period, moves to a different location in the system to receive EMR exposure for a second time period.
  • SOFCs solid oxide fuel cells
  • AM additive manufacturing
  • AM is also referred as additive fabrication, additive processes, additive techniques, additive layer manufacturing, layer manufacturing, and freeform fabrication.
  • Some examples of AM are extrusion, photopolymerization, powder bed fusion, material jetting, binder jetting, directed energy deposition, lamination, direct metal laser sintering (DMLS), selective laser sintering (SLS), selective laser melting (SLM), directed energy deposition (DED), laser metal deposition (LMD), electron beam (EBAM), and metal binder jetting.
  • DMLS direct metal laser sintering
  • SLS selective laser sintering
  • SLM selective laser melting
  • DED directed energy deposition
  • LMD laser metal deposition
  • EBAM electron beam
  • a 3D printer is a type of AM machine (AMM).
  • An inkjet printer or ultrasonic inkjet printer are also AMM's.
  • the invention is a method of making a fuel cell comprising (a) producing an anode using an additive manufacturing machine (AMM); (b) creating an electrolyte using the AMM; and (c) making a cathode using the AMM.
  • AMM additive manufacturing machine
  • the anode, the electrolyte, and the cathode are assembled into a fuel cell utilizing the AMM.
  • the fuel cell is formed using only the AMM.
  • steps (a), (b), and (c) exclude tape casting and exclude screen printing.
  • the method excludes compression in assembling.
  • the layers are deposited one on top of another and as such assembling is accomplished at the same time as deposition.
  • the method of this disclosure is useful in making planar fuel cells.
  • the method of this disclosure is useful in making fuel cells, wherein electrical current flow is perpendicular to the electrolyte in the lateral direction when the fuel cell is in use.
  • the interconnect, the anode, the electrolyte, and the cathode are formed layer on layer, for example, printed layer on layer. It is important to note that, within the scope of the invention, the order of forming these layers can be varied. In other words, either the anode or the cathode can be formed before the other. Naturally, the electrolyte is formed so that it is between the anode and the cathode.
  • the barrier layer(s), catalyst layer(s) and interconnect(s) are formed so as to lie in the appropriate position within the fuel cell to perform their functions.
  • each of the interconnect, the anode, the electrolyte, and the cathode has six faces.
  • the anode is printed on the interconnect and is in contact with the interconnect;
  • the electrolyte is printed on the anode and is in contact with the anode;
  • the cathode is printed on the electrolyte and is in contact with the electrolyte.
  • Each print is sintered, for example, using EMR.
  • the method comprises making at least one barrier layer using the AMM.
  • the at least one barrier layer is used between the electrolyte and the cathode or between the electrolyte and the anode or both.
  • the at least one barrier layer is assembled with the anode, the electrolyte, and the cathode using the AMM.
  • no barrier layer is utilized in the fuel cell.
  • the method comprises making an interconnect using the AMM.
  • the interconnect is assembled with the anode, the electrolyte, and the cathode using the AMM.
  • the AMM forms a catalyst and incorporates said catalyst into the fuel cell.
  • the anode, the electrolyte, the cathode, and the interconnect are made at a temperature above 100 °C.
  • the method comprises heating the fuel cell, wherein said fuel cell comprises the anode, the electrolyte, the cathode, the interconnect, and optionally at least one barrier layer.
  • the fuel cell comprises a catalyst.
  • the method comprises heating the fuel cell to a temperature above 500 °C.
  • the fuel cell is heated using EMR or oven curing.
  • the AMM utilizes a multi-nozzle additive manufacturing method.
  • the multi-nozzle additive manufacturing method comprises nanoparticle jetting.
  • a first nozzle delivers a first material.
  • a second nozzle delivers a second material.
  • a third nozzle delivers a third material.
  • particles of a fourth material are placed in contact with a partially constructed fuel cell and bonded to the partially constructed fuel cell using a laser
  • the anode, or the cathode, or the electrolyte comprises a first, second, third, or fourth material.
  • the AMM performs multiple additive manufacturing techniques.
  • the additive manufacturing techniques comprise extrusion,
  • additive manufacturing is a deposition technique comprising material jetting, binder jetting, inkjet printing, aerosol jetting, or aerosol jet printing, vat photopolymerization, powder bed fusion, material extrusion, directed energy deposition, sheet lamination, ultrasonic inkjet printing, or combinations thereof.
  • AMM additive manufacturing machine
  • anode, the electrolyte, the cathode, and the interconnect form a first fuel cell; (e) repeating steps (a)-(d) to make a second fuel cell; and (f) assembling the first fuel cell and the second fuel cell into a fuel cell stack.
  • the first fuel cell and the second fuel cell are formed from the anode, the electrolyte, the cathode, and the interconnect utilizing the AMM.
  • the fuel cell stack is formed using only the AMM.
  • steps (a)-(f) exclude tape casting and exclude screen printing.
  • the method comprises making at least one barrier layer using the AMM.
  • the at least one barrier layer is used between the electrolyte and the cathode or between the electrolyte and the anode or both for the first fuel cell and the second fuel cell.
  • steps (a)-(d) are performed at a temperature above 100 °C.
  • steps (a)-(d) are performed at a temperature from 100 °C to 500 °C.
  • the AMM makes a catalyst and incorporates said catalyst into the fuel cell stack.
  • the method comprises heating the fuel cell stack.
  • the method comprises heating the fuel cell stack to a temperature above 500 °C.
  • the fuel cell stack is heated using EMR and/or oven curing.
  • the laser has a laser beam, wherein said laser beam is expanded to create a heating zone with uniform power density.
  • the laser beam is expanded by the use of one or more mirrors.
  • each layer of the fuel cell is EMR cured separately.
  • a combination of fuel cell layers is EMR cured together.
  • the first fuel cell is EMR cured, assembled with the second fuel cell, and then the second fuel cell is EMR cured.
  • the first fuel cell is assembled with the second fuel cell, and then the first fuel cell and the second fuel cell are EMR cured separately.
  • the first fuel cell and the second fuel cell are EMR cured separately, and then the first fuel cell is assembled with the second fuel cell to form a fuel cell stack. In an embodiment, the first fuel cell is assembled with the second fuel cell to form a fuel cell stack, and then the fuel cell stack is EMR cured.
  • a method of making a multiplicity of fuel cells comprising (a) producing a multiplicity of anodes simultaneously using an additive manufacturing machine (AMM); (b) creating a multiplicity of electrolytes using the AMM simultaneously; and (c) making a multiplicity of cathodes using the AMM simultaneously.
  • AMM additive manufacturing machine
  • the anodes, the electrolytes, and the cathodes are assembled into fuel cells utilizing the AMM simultaneously.
  • the fuel cells are formed using only the AMM.
  • the method comprises making at least one barrier layer using the AMM for each of the multiplicity of fuel cells simultaneously.
  • said at least one barrier layer is used between the electrolyte and the cathode or between the electrolyte and the anode or both.
  • said at least one barrier layer is assembled with the anode, the electrolyte, and the cathode using the AMM for each fuel cell.
  • the method comprises making an interconnect using the AMM for each of the multiplicity of fuel cells simultaneously. In an embodiment, said interconnect is assembled with the anode, the electrolyte, and the cathode using the AMM for each fuel cell.
  • the AMM forms a catalyst for each of the multiplicity of fuel cells
  • the multiplicity of fuel cells is 20 fuel cells or more.
  • the AMM uses different nozzles to jet/print different materials at the same time.
  • a first nozzle makes an anode for fuel cell 1
  • a second nozzle makes a cathode for fuel cell 2
  • a third nozzle makes an electrolyte for fuel cell 3, at the same time.
  • a first nozzle makes an anode for fuel cell 1
  • a second nozzle makes a cathode for fuel cell 2
  • a third nozzle makes an electrolyte for fuel cell 3
  • a fourth nozzle makes an interconnect for fuel cell 4, at the same time.
  • an additive manufacturing machine comprising a chamber, wherein manufacturing of fuel cells takes place, wherein said chamber is able to withstand a temperature of at least 300 °C.
  • said chamber enables production of the fuel cells.
  • said chamber enables heating of the fuel cells in situ, meaning that the fuel cells are heated in the same machine, and preferably in the same location in that machine as the components of the fuel cell were deposited.
  • said chamber is heated by laser, or electromagnetic
  • said heating element comprises a heating surface or a heating coil or a heating rod.
  • said chamber is configured to apply pressure to the fuel cells inside. In an embodiment, the pressure is applied via a moving element associated with the chamber. In an embodiment, said moving element is a moving stamp or plunger. In an embodiment, said chamber is configured to withstand pressure. In an embodiment, said chamber is configured to be pressurized by a fluid or de pressurized. In an embodiment, said fluid in the chamber is changed or replaced. [76] In some cases, the chamber is enclosed. In some cases, the chamber is sealed. In some cases, the chamber is open. In some cases, the chamber is a platform without top and side walls.
  • 601 represents deposition nozzles or material jetting nozzles
  • 602 represents EMR source, e.g., xenon lamp
  • 603 represents object being formed
  • 604 represents chamber as a part of an AMM.
  • the chamber or receiver 604 is configured to receive both deposition from nozzles and radiation from an EMR source.
  • deposition nozzles 601 are movable.
  • the chamber or receiver 604 is movable.
  • the EMR source 602 is movable.
  • the object comprises a catalyst, a catalyst support, a catalyst composite, an anode, a cathode, an electrolyte, an electrode, an interconnect, a seal, a fuel cell, an electrochemical gas producer, an electrolyser, an electrochemical compressor, a reactor, a heat exchanger, a vessel, or combinations thereof.
  • Additive Manufacturing techniques suitable for this disclosure comprise extrusion, photopolymerization, powder bed fusion, material jetting, binder jetting, directed energy deposition, and lamination.
  • Additive Manufacturing is extrusion additive manufacturing. Extrusion additive manufacturing involves the spatially controlled deposition of material (e.g., thermoplastics). It is also referred to as fused filament fabrication (FFF) or fused deposition modeling (FDM) in this disclosure.
  • FFF fused filament fabrication
  • FDM fused deposition modeling
  • Additive Manufacturing is photopolymerization, i.e., photopolymerization
  • SLA stereolithography
  • Additive Manufacturing is Powder bed fusion (PBF).
  • PBF AM processes build objects by melting powdered feedstock, such as a polymer or metal. PBF processes begin by spreading a thin layer of powder across the build area. Cross sections are then melted a layer at a time, most often using a laser, electron beam, or intense infrared lamps.
  • PBF of metals is selective laser melting (SLM) or electron beam melting (EBM).
  • PBF of polymers is selective laser sintering (SLS).
  • SLS systems print thermoplastic polymer materials, polymer composites, or ceramics.
  • SLM systems are suitable for a variety of pure metals and alloys, wherein the alloys are compatible with the rapid solidification that occurs in SLM.
  • Additive Manufacturing is material jetting. Additive manufacturing by material jetting is accomplished by depositing small drops (or droplets) of material, with spatial control. In various embodiments, material jetting is performed three dimensionally (3D) or two dimensionally (2D) or both. In an embodiment, 3D jetting is accomplished layer by layer. In an embodiment, print preparation converts the computer-aided design (CAD), along with specifications of material composition, color, and other variables to the printing instructions for each layer.
  • CAD computer-aided design
  • Additive Manufacturing utilizes binder jetting.
  • Binder jetting AM involves inkjet deposition of a liquid binder onto a powder bed.
  • binder jetting combines physics of other AM processes: spreading of powder to make the powder bed
  • Binder Jetting does not require any support structures.
  • the built parts lie in the bed of not bonded powder.
  • the entire build volume can therefore be filled with several parts, including stacking and pyramiding of parts. These are then all produced together. Binder Jetting works with almost any material that is available in powder form.
  • Aerosol Jet Printing (sometimes known as Maskless Mesoscale Materials Deposition or M3D)[24] begins with atomization of an ink, such as by ultrasonic or pneumatic means, typically producing droplets on the order of one to two micrometres in diameter. These droplets then preferably flow through a virtual impactor which is designed to deflect the droplets having lower momentum away from the stream. This step can help maintain a tight droplet size distribution.
  • the droplets are entrained in a gas stream and delivered to the print head.
  • an annular flow of clean gas is preferably introduced around the aerosol stream to focus the droplets into a tightly collimated beam of material.
  • the combined gas streams exit the print head through a converging nozzle that compresses the aerosol stream to a diameter as small as 10 pm.
  • the jet of droplets exits the print head at high velocity, such as ⁇ 50 meters/second, and impinges upon the substrate.
  • the aerosol jet printing process is relatively gentle, meaning that substrate damage typically does not occur and there is generally minimal splatter or overspray from the droplets. Once deposition is complete, the printed ink can require post treatment to attain final electrical and mechanical properties.
  • Additive Manufacturing is directed energy deposition (DED).
  • the DED process uses a directed flow of powder or a wire feed, along with an energy intensive source such as laser, electric arc, or electron beam.
  • DED is a direct-write process, wherein the location of material deposition is determined by movement of the deposition head, which allows large metal structures to be built without the constraints of a powder bed.
  • Additive Manufacturing is Lamination AM, or Laminated Object Manufacturing (LOM).
  • LOM Laminated Object Manufacturing
  • consecutive layers of sheet material are
  • the method of this disclosure manufactures a fuel cell or a fuel cell stack using one AMM.
  • the AMM of this disclosure preferably performs both extrusion and ink jetting to manufacture a fuel cell or fuel cell stack.
  • Extrusion is used to manufacture thicker layers of a fuel cell, such as, the anode and/or the cathode.
  • Ink jetting is used to manufacture thin layers of a fuel cell.
  • Ink jetting is used to manufacture the electrolyte.
  • the AMM operates at temperature ranges sufficient to enable curing in the AMM itself. Such temperature ranges are 100 °C or above, such as 100 °C - S00 °C or 100 °C - 500 °C.
  • the aqueous ink comprises an aqueous solvent (e.g., water, deionized water), particles, a dispersant, and a surfactant.
  • the aqueous ink comprises an aqueous solvent (e.g., water, deionized water), particles, a dispersant, a surfactant, but no polymeric binder.
  • the aqueous ink optionally comprises a co-solvent, such as an organic miscible solvent
  • the dispersant is an electrostatic dispersant, a steric dispersant, an ionic dispersant, a non-ionic dispersant, or a combination thereof.
  • the surfactant is preferably non ionic, such as an alcohol alkoxylate, an alcohol ethoxylate.
  • the non-aqueous ink comprises an organic solvent (e.g., methanol, ethanol, isopropyl alcohol, butanol) and particles.
  • CGO powder is mixed with water to form an aqueous ink with a dispersant added and a surfactant added but with no polymeric binder added.
  • the CGO fraction based on mass is in the range of from 10 wt% to 25 wt%.
  • CGO powder is mixed with ethanol to form a non-aqueous ink with polyvinyl butaryl added.
  • the CGO fraction based on mass is in the range of from 3 wt% to 30 wt%.
  • LSCF is mixed with n-butanol or ethanol to form a non-aqueous ink with polyvinyl butaryl added.
  • the LSCF fraction based on mass is in the range of from 10 wt% to 40 wt%.
  • YSZ particles are mixed with water to form an aqueous ink with a dispersant added and a surfactant added but with no polymeric binder added.
  • the YSZ fraction based on mass is in the range of from 3 wt% to 40 wt%.
  • NiO particles are mixed with water to form an aqueous ink with a dispersant added and a surfactant added but with no polymeric binder added.
  • the NiO fraction based on mass is in the range of from 5 wt% to 25 wt%.
  • LSCF or LSM particles are dissolved in a solvent, wherein the solvent is water or an alcohol (e.g., butanol) or a mixture of alcohols.
  • LSCF is deposited (e.g., printed) into a layer.
  • a xenon lamp irradiates the LSCF layer with EMR to sinter the LSCF.
  • the flash lamp is a 10 kW unit applied at a voltage of 400V and a frequency of 10 Hz for a total exposure duration of 1000 ms.
  • YSZ particles are mixed with a solvent, wherein the solvent is water (e.g., de-ionized water) (e.g., de-ionized water) or an alcohol (e.g., butanol) or a mixture of alcohols.
  • the solvent is water (e.g., de-ionized water) (e.g., de-ionized water) or an alcohol (e.g., butanol) or a mixture of alcohols.
  • Organic solvents other than alcohols may also be used.
  • the solvent may include water (e.g., de-ionized water), organic solvents (e.g. mono-, di-, or tri ethylene glycols or higher ethylene glycols, propylene glycol, 1,4-butanediol or ethers of such glycols, thiodiglycol, glycerol and ethers and esters thereof, polyglycerol, mono-, di-, and tri ethanolamine, propanolamine, N,N-dimethylformamide, dimethyl sulfoxide,
  • water e.g., de-ionized water
  • organic solvents e.g. mono-, di-, or tri ethylene glycols or higher ethylene glycols, propylene glycol, 1,4-butanediol or ethers of such glycols, thiodiglycol, glycerol and ethers and esters thereof, polyglycerol, mono-, di-, and tri ethanolamine, propanolamine, N
  • CGO particles are dissolved in a solvent, wherein the solvent is water (e.g., de-ionized water) or an alcohol (e.g., butanol) or a mixture of alcohols. Organic solvents other than alcohols may also be used.
  • the solvent is water (e.g., de-ionized water) or an alcohol (e.g., butanol) or a mixture of alcohols.
  • Organic solvents other than alcohols may also be used.
  • CGO is used as barrier layer for LSCF.
  • YSZ may also be used as a barrier layer for LSM.
  • no polymeric binder is added to the aqueous inks.
  • a method of making a fuel cell comprises using only one additive manufacturing machine (AMM) to manufacture a fuel cell, wherein the fuel cell comprises an anode, electrolyte, and a cathode.
  • AMM additive manufacturing machine
  • the fuel cell comprises at least one barrier layer, for example, between the electrolyte and the cathode, or between the electrolyte and the cathode, or both.
  • the at least one barrier layer is also made by the same single AMM.
  • the AMM also produces an interconnect and assembles the interconnect with the anode, the cathode, the barrier layer(s), and the electrolyte.
  • Such manufacturing method and system are applicable not only to making fuel cells but also for making any electrochemical device. The following discussion takes fuel cell as an example, but any reactor or catalyst is within the scope of this disclosure.
  • the single AMM makes a first fuel cell, wherein the fuel cell comprises the anode, the electrolyte, the cathode, the at least one barrier layer, and the interconnect.
  • the single AMM makes a second fuel cell.
  • the single AMM assembles the first fuel cell with the second fuel cell to form a fuel cell stack.
  • the production using AMM is repeated as many times as desired; and a fuel cell stack is assembled using the AMM.
  • the various layers of the fuel cell are produced by the AMM above ambient temperature, for example, above 100 °C, from 100 °C to 500 °C, from 100 °C to 300 °C.
  • the fuel cell or fuel cell stack is heated after it is formed/assembled. In an embodiment, the fuel cell or fuel cell stack is heated at a temperature above 500 °C. In an embodiment, the fuel cell or fuel cell stack is heated at a temperature from 500 °C to 1500 °C.
  • the AMM comprises a chamber where the manufacturing of fuel cells takes place. This chamber is able to withstand high temperature to enable the production of the fuel cells. In an embodiment, this high temperature is at least 300 °C. In an embodiment, this high temperature is at least 500 °C. In an embodiment, this high
  • this high temperature is at least 1500 °C.
  • this chamber also enables heating of the fuel cells to take place in the chamber.
  • Various heating methods are applied, such as laser heating/curing, electromagnetic wave heating, hot fluid heating, or heating element associated with the chamber.
  • the heating element may be a heating surface or a heating coil or a heating rod and is associated with the chamber such that the content in the chamber is heated to the desired temperature range.
  • the chamber of the AMM is able to apply pressure to the fuel cell(s) inside, for example, via a moving element (e.g., a moving stamp or plunger).
  • the chamber of the AMM is able to withstand pressure.
  • the chamber can be pressurized by a fluid and de-pressurized as desired.
  • the fluid in the chamber can also be changed/replaced as needed.
  • the fuel cell or fuel cell stack is heated using EMR.
  • the fuel cell or fuel cell stack is heated using oven curing.
  • the laser beam is expanded (for example, by the use of one or more mirrors) to create a heating zone with uniform power density.
  • each layer of the fuel cell is EMR cured separately.
  • a combination of fuel cell layers is EMR cured separately, for example, a combination of the anode, the electrolyte, and the cathode layers.
  • a first fuel cell is EMR cured, assembled with a second fuel cell, and then the second fuel cell is EMR cured.
  • a first fuel cell is assembled with a second fuel cell, and then the first fuel cell and the second fuel cell are EMR cured separately.
  • a first fuel cell is assembled with a second fuel cell to form a fuel cell stack, and then the fuel cell stack is EMR cured. The sequence of laser heating/curing and assembling is applicable to all other heating methods.
  • the AMM produces each layer of a multiplicity of fuel cells simultaneously. In an embodiment, the AMM assembles each layer of a multiplicity of fuel cells simultaneously. In an embodiment, heating of each layer or heating of a combination of layers of a multiplicity of fuel cells takes place simultaneously. All the discussion and all the features herein for a fuel cell or a fuel cell stack are applicable to the production, assembling, and heating of the multiplicity of fuel cells. In an embodiment, a multiplicity of fuel cells is 20 or more. In an embodiment, a multiplicity of fuel cells is 50 or more. In an embodiment, a multiplicity of fuel cells is 80 or more. In an embodiment, a multiplicity of fuel cells is 100 or more. In an embodiment, a multiplicity of fuel cells is 500 or more.
  • a multiplicity of fuel cells is 800 or more. In an embodiment, a multiplicity of fuel cells is 1000 or more. In an embodiment, a multiplicity of fuel cells is 5000 or more. In an embodiment, a multiplicity of fuel cells is 10,000 or more.
  • the treatment process comprises exposing a sample to a source of electromagnetic radiation (EMR).
  • EMR treats a sample having a first material.
  • the EMR has a peak wavelength ranging from 10 to 1500 nm.
  • the EMR has a minimum energy density of 0.1 Joule/cm 2 .
  • the EMR has a burst frequency of 10 4 -1000 Hz or 1-1000 Hz or 10-1000 Hz.
  • the EMR has an exposure distance of no greater than 50 mm.
  • the EMR has an exposure duration no less than 0.1 ms or 1 ms.
  • the EMR is applied with a capacitor voltage of no less than 100V.
  • a single pulse of EMR is applied with an exposure distance of about 10 mm and an exposure duration of 5-20 ms.
  • multiple pulses of EMR are applied at a burst frequency of 100Hz with an exposure distance of about 10 mm and an exposure duration of 5-20 ms.
  • the EMR consists of one exposure.
  • the EMR comprises no greater than 10 exposures, or no greater than 100 exposures, or no greater than 1000 exposures, or no greater than 10,000 exposures.
  • metals and ceramics are sintered almost instantly (milliseconds for «10 microns) using pulsed light.
  • the sintering temperature is controlled to be in the range of from 100 °C to 2000 °C.
  • the sintering temperature is tailored as a function of depth.
  • the surface temperature is 1000 °C and the sub-surface is kept at 100 °C, wherein the sub surface is 100 microns below the surface.
  • the material suitable for this treatment process includes Yttria-stabilized zirconia (YSZ), 8YSZ (8mol% YSZ powder), Yttirum, Zirconium, gadolinia-doped ceria (GDC or CGO), Samaria-doped ceria (SDC), Scandia-stabilized zirconia (SSZ), Lanthanum strontium manganite (LSM), Lanthanum Strontium Cobalt Ferrite (LSCF), Lanthanum Strontium Cobaltite (LSC), Lanthanum Strontium Gallium Magnesium Oxide (LSGM), Nickel, NiO, NiO-YSZ, Cu-CGO, Cu 2 0, CuO, Cerium, copper, silver, crofer, steel, lanthanum chromite, doped lanthanum chromite, ferritic steel, stainless steel, or combinations thereof.
  • YSZ Yttria-stabilized zirconia
  • 8YSZ 8mol% Y
  • This treatment process is applicable in the manufacturing process of a fuel cell.
  • a layer of a fuel cell (anode, cathode, electrolyte, seal, catalyst) is treated using the process of this disclosure to be heated, cured, sintered, sealed, alloyed, foamed, evaporated, restructured, dried, or annealed.
  • a portion of a layer of a fuel cell (anode, cathode, electrolyte, seal, catalyst) is treated using the process of this disclosure to be heated, cured, sintered, sealed, alloyed, foamed, evaporated, restructured, dried, or annealed.
  • a combination of layers of a fuel cell is treated using the process of this disclosure to be heated, cured, sintered, sealed, alloyed, foamed, evaporated, restructured, dried, or annealed, wherein the layers may be a complete layer or a partial layer.
  • the treatment process of this disclosure is preferably rapid, with the treatment duration varied from microseconds to milliseconds.
  • the treatment duration is accurately controlled.
  • the treatment process of this disclosure produces fuel cell layers that have no crack or have minimal cracking.
  • the treatment process of this disclosure controls the power density or energy density in the treatment volume of the material being treated.
  • the treatment volume is accurately controlled.
  • the treatment process of this disclosure provides the same energy density or different energy densities in a treatment volume.
  • the treatment process of this disclosure provides the same treatment duration or different treatment durations in a treatment volume.
  • the treatment process of this disclosure provides simultaneous treatment for one or more treatment volumes.
  • the treatment process of this disclosure provides simultaneous treatment for one or more fuel cell layers or partial layers or combination of layers.
  • the treatment volume is varied by changing the treatment depth.
  • a first portion of a treatment volume is treated by electromagnetic radiation of a first wavelength; a second portion of the treatment volume is treated by electromagnetic radiation of a second wavelength.
  • the first wavelength is the same as the second wavelength.
  • the first wavelength is different from the second wavelength.
  • the first portion of a treatment volume has a different energy density from the second portion of the treatment volume.
  • the first portion of a treatment volume has a different treatment duration from the second portion of the treatment volume.
  • the EMR has a broad emission spectrum so that the desired effects are achieved for a wide range of materials having different absorption characteristics.
  • absorption of electromagnetic radiation refers to the process, wherein the energy of a photon is taken up by matter, such as the electrons of an atom.
  • the electromagnetic energy is transformed into internal energy of the absorber, for example, thermal energy.
  • the EMR spectrum extends from the deep ultraviolet (UV) range to the near infrared (IR) range, with peak pulse powers at 220 nm wavelength.
  • the power of such EMR is on the order of Megawatts.
  • Such EMR sources perform tasks such as breaking chemical bonds, sintering, ablating or sterilizing.
  • the EMR has an energy density of no less than 0.1, 1, or 10
  • the EMR has a power output of no less than 1 watt (W), 10 W, 100 W, 1000 W.
  • the EMR delivers power to the sample of no less than 1 W, 10 W, 100 W, 1000 W.
  • such EMR exposure heats the material in the sample.
  • the EMR has a range or a spectrum of different wavelengths.
  • the treated sample is at least a portion of an anode, cathode, electrolyte, catalyst, barrier layer, or interconnect of a fuel cell.
  • the peak wavelength of the EMR is between 50 and 550 nm or between 100 and 300 nm.
  • the absorption of at least a portion of the sample for at least one frequency of the EMR between 10 and 1500 nm is no less than 30% or no less than 50%.
  • the absorption of at least a portion of the sample for at least one frequency between 50 and 550 nm is no less than 30% or no less than 50%.
  • the absorption of at least a portion of the sample for at least one frequency between 100 and 300 nm is no less than 30% or no less than 50%.
  • Sintering is the process of compacting and forming a solid mass of material by heat or pressure without melting it to the point of liquefaction.
  • the sample under EMR exposure is sintered but not melted.
  • the EMR is UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam, microwave.
  • the sample is exposed to the EMR for no less than 1 microsecond, no less than 1 millisecond.
  • the sample is exposed to the EMR for less than 1 second at a time or less than 10 seconds at a time.
  • the sample is exposed to the EMR for less than 1 second or less than 10 seconds.
  • the sample is exposed to the EMR repeatedly, for example, more than 1 time, more than 3 times, more than 10 times.
  • the sample is distanced from the source of the EMR for less than 50 cm, less than 10 cm, less than 1 cm, or less than 1 mm.
  • a second material is added to or placed on to the first material.
  • the second material is the same as the first material.
  • the second material is exposed to the EMR.
  • a third material is added.
  • the third material is exposed to the EMR.
  • the first material comprises YSZ, 8YSZ, Yttirum, Zirconium, GDC, SDC, LSM, LSCF, LSC, Nickel, NiO, Cerium.
  • the second material comprises graphite.
  • the electrolyte, anode, or cathode comprises a second material.
  • the volume fraction of the second material in the electrolyte, anode, or cathode is less than 20%, 10%, 3%, or 1%.
  • the absorption rate of the second material for at least one frequency e.g., between 10 and 1500 nm or between 100 and 300 nm or between 50 and 550 nm) is greater than 30% or greater than 50%.
  • one or a combination of parameters are controlled, wherein such parameters include distance between the EMR source and the sample, the energy density of the EMR, the spectrum of the EMR, the voltage of the EMR, the duration of exposure, the burst frequency, and the number of EMR exposures.
  • these parameters are controlled to minimize the formation of cracks in the sample.
  • the EMR energy is delivered to a surface area of no less than 1 mm2, or no less than 1 cm2, or no less than 10 cm2, or no less than 100 cm2.
  • at least a portion of an adjacent material is heated at least in part by conduction of heat from the first material.
  • the layers of the fuel cell e.g., anode, cathode, electrolyte
  • they are no greater than 30 microns, no greater than 10 microns, or no greater than 1 micron.
  • the first material of the sample is in the form of a powder, sol gel, colloidal suspension, hybrid solution, or sintered material.
  • the second material may be added by vapor deposition.
  • the second material coats the first material.
  • the second material reacts with light, e.g. focused light, as by a laser and sinter or anneal with the first material.
  • the preferred treatment process of this disclosure enables rapid manufacturing of fuel cells by eliminating traditional, costly, time consuming, expensive sintering processes and replacing them with rapid, in-situ methods that allow continuous manufacturing of the layers of a fuel cell in a single machine if desired. This process also shortens sintering time from hours and days to seconds or milliseconds or even microseconds.
  • this treatment method is used in combination with
  • This preferred treatment method enables tailored and controlled heating by tuning EMR characteristics (such as, wavelengths, energy density, burst frequency, and exposure duration) combined with controlling thicknesses of the layers of the sample and heat conduction into adjacent layers to allow each layer to sinter, anneal, or cure at each desired target
  • such particle size distribution comprises D10 and D90, wherein 10% of the particles have a diameter no greater than D10 and 90% of the particles have a diameter no greater than D90, wherein D90/D10 is in the range of from 1.5 to 100.
  • such particle size distribution is bimodal such that the average particle size in the first mode is at least 5 times the average particle size in the second mode.
  • such particle size distribution comprises D50, wherein 50% of the particles have a diameter no greater than D50, wherein D50 is no greater than 100 nm.
  • the sintering processes utilize electromagnetic radiation (EMR), or plasma, or a furnace, or hot fluid, or a heating element, or combinations thereof preferably, the sintering processes utilize electromagnetic radiation (EMR).
  • EMR electromagnetic radiation
  • an EMR source just sufficient to sinter a material has power capacity P.
  • the material is sintered with EMR sources having much less power capacity, e.g., 50% P or less, 40% P or less, 30% P or less, 20% P or less, 10% P or less, 5% P or less.
  • a method of sintering a material comprising mixing particles with a liquid to form a dispersion, wherein the particles have a particle size distribution comprising D10 and D90, wherein 10% of the particles have a diameter no greater than D10 and 90% of the particles have a diameter no greater than D90, wherein D90/D10 is in the range of from 1.5 to 100; depositing the dispersion on a substrate to form a layer; and treating the layer to cause at least a portion of the particles to sinter.
  • the particle size distribution is a number distribution determined by dynamic light scattering.
  • Dynamic light scattering is a technique that can be used to determine the size distribution profile of small particles in a dispersion or suspension.
  • temporal fluctuations are typically analyzed by means of the intensity or photon auto-correlation function (also known as photon correlation spectroscopy or quasi-elastic light scattering).
  • the autocorrelation function (ACF) usually decays starting from zero delay time, and faster dynamics due to smaller particles lead to faster decorrelation of scattered intensity trace. It has been shown that the intensity ACF is the Fourier transformation of the power spectrum, and therefore the DLS measurements can be equally well performed in the spectral domain.
  • the particle size distribution is determined by transmission electron microscopy (TEM).
  • TEM is a microscopy technique in which a beam of electrons is transmitted through a specimen to form an image.
  • the specimen is most often a suspension on a grid.
  • An image is formed from the interaction of the electrons with the sample as the beam is transmitted through the specimen.
  • the image is then magnified and focused onto an imaging device, such as a fluorescent screen or a sensor such as a scintillator attached to a charge- coupled device.
  • a method of sintering a material comprising mixing particles with a liquid to form a dispersion, wherein the particles have a particle size distribution comprising D50, wherein 50% of the particles have a diameter no greater than D50, wherein D50 is no greater than 100 nm; depositing the dispersion on a substrate to form a layer; and treating the layer to cause at least a portion of the particles to sinter.
  • D50 is no greater than 50 nm, or no greater than 30 nm, or no greater than 20 nm, or no greater than 10 nm, or no greater than 5 nm.
  • the layer has a thickness of no greater than 1 mm or no greater than 500 microns or no greater than 300 microns or no greater than 100 microns or no greater than 50 microns.
  • depositing comprises material jetting, binder jetting, inkjet printing, aerosol jetting, or aerosol jet printing, vat photopolymerization, powder bed fusion, material extrusion, directed energy deposition, sheet lamination, ultrasonic inkjet printing, or combinations thereof.
  • said liquid comprises water and at least one organic solvent having a lower boiling point than water and miscible with water.
  • said liquid comprises water, a surfactant, a dispersant, and no polymeric binder.
  • said liquid comprises one or more organic solvents and no water.
  • the particles comprise Cu, CuO, CU2O, Ag, Ag 2 0, Au, AU2O, AU2O3, titanium, Yttria- stabilized zirconia (YSZ), 8YSZ (8mol% YSZ powder), Yttirum, Zirconium, gadolinia-doped ceria (GDC or CGO), Samaria-doped ceria (SDC), Scandia-stabilized zirconia (SSZ), Lanthanum strontium manganite (LSM), Lanthanum Strontium Cobalt Ferrite (LSCF), Lanthanum Strontium Cobaltite (LSC), Lanthanum Strontium Gallium Magnesium Oxide (LSGM), Nickel (Ni), NiO, NiO- YSZ, Cu-CGO, cerium, crofer, steel, lanthanum chromite, doped lanthanum chromite, ferritic steel, stainless steel, or combinations thereof.
  • YSZ Yttria
  • DIO is in the range of from 5 nm to 50 nm or from 5 nm to 100 nm or from 5 nm to 200 nm.
  • D90 is in the range of from 50 nm to 500 nm or from 50 nm to 1000 nm.
  • D90/D10 is in the range of from 2 to 100 or from 4 to 100 or from 2 to 20 or from 2 to 10 or from 4 to 20 or from 4 to 10.
  • the method comprises drying the dispersion after depositing.
  • drying comprises heating the dispersion before deposition, heating the substrate that is contact with the dispersion, or combination thereof.
  • drying takes place for a period in the range of from 1 ms to 1 min or from 1 s to 30 s or from 3 s to 10 s.
  • the dispersion is deposited at a temperature in the range of from 40°C to 100°C or from 50°C to 90°C or from 60°C to 80°C or about 70°C.
  • treating comprises the use of electromagnetic radiation (EMR), or a furnace, or plasma, or hot fluid, or a heating element, or combinations thereof.
  • EMR electromagnetic radiation
  • the EMR comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam, microwave.
  • the EMR consists of one exposure.
  • the EMR has an exposure frequency of 10-4-1000 Hz or 1- 1000 Hz or 10-1000 Hz.
  • the EMR has an exposure distance of no greater than 50 mm.
  • the EMR has an exposure duration no less than 0.1 ms or 1 ms.
  • the EMR is applied with a capacitor voltage of no less than 100V.
  • a fuel cell is an electrochemical apparatus that converts the chemical energy from a fuel into electricity through an electrochemical reaction.
  • fuel cells e.g., proton-exchange membrane fuel cells (PEMFCs), solid oxide fuel cells (SOFCs).
  • a fuel cell typically comprises an anode, a cathode, an electrolyte, an interconnect, optionally a barrier layer and/or optionally a catalyst. Both the anode and the cathode are electrodes.
  • the listings of material for the electrodes, the electrolyte, and the interconnect in a fuel cell are applicable in some cases to the EC gas producer and the EC compressor. These listings are only examples and not limiting.
  • anode material and cathode material are also not limiting because the function of the material during operation (e.g., whether it is oxidizing or reducing) determines whether the material is used as an anode or a cathode.
  • Figures 1-5 illustrate various embodiments of the components in a fuel cell or a fuel cell stack.
  • the anode, cathode, electrolyte, and interconnect are cuboids or rectangular prisms.
  • 201 schematically represents the anode; 202 represents the cathode; 203 represents the electrolyte; and 204 represents the barrier layers.
  • Figure 5 depicts two fuel cells in a fuel cell stack.
  • Item 501 schematically represents the anode; 502 represents the cathode; 503 represents the electrolyte; 504 represents the barrier layers; 505 represents the catalyst; and 506 represents the interconnect.
  • Two fuel cell repeat units or two fuel cells form a stack as illustrated. As is seen, on one side the interconnect is in contact with the largest surface of the cathode of the top fuel cell (or fuel cell repeat unit) and on the opposite side the interconnect is in contact with the largest surface of the catalyst (optional) or the anode of the bottom fuel cell (or fuel cell repeat unit).
  • repeat units or fuel cells are connected in parallel by being stacked atop one another and sharing an interconnect in between via direct contact with the interconnect rather than via electrical wiring.
  • This kind of configuration is in contrast to segmented-in-series (SIS) type fuel cells.
  • SIS segmented-in-series
  • the unique manufacturing methods as discussed herein have allowed the making of ultra-thin fuel cells and fuel cell stacks.
  • the fuel cell has at least one thick layer per repeat unit, like the anode (an anode-supported fuel cell) or the interconnect (an interconnect-supported fuel cell).
  • the pressing or compression step is typically necessary to assemble the fuel cell components to achieve gas tightness and/or proper electrical contact in traditional manufacturing processes.
  • the thick layers are necessary not only because traditional methods (like tape casting) cannot produce ultra-thin layers but also because the layers have to be thick to endure the pressing or compression step.
  • the preferred manufacturing methods of this disclosure have eliminated the need for pressing or compression.
  • the preferred manufacturing methods of this disclosure have also enabled the making of ultra-thin layers.
  • the multiplicity of the layers in a fuel cell or a fuel cell stack provides sufficient structural integrity for proper operation when they are made according to this disclosure.
  • a fuel cell comprising an anode no greater than 1 mm or 500 microns or 300 microns or 100 microns or 50 microns or no greater than 25 microns in thickness, a cathode no greater than 1 mm or 500 microns or 300 microns or 100 microns or 50 microns or no greater than 25 microns in thickness, and an electrolyte no greater than 1 mm or 500 microns or 300 microns or 100 microns or 50 microns or 30 microns in thickness.
  • the fuel cell comprises an interconnect having a thickness of no less than 50 microns.
  • a fuel cell comprises an anode no greater than 25 microns in thickness, a cathode no greater than 25 microns in thickness, and an electrolyte no greater than 10 microns or 5 microns in thickness.
  • the fuel cell comprises an interconnect having a thickness of no less than 50 microns.
  • the interconnect has a thickness of from 50 microns to 5 cm.
  • a fuel cell comprises an anode no greater than 100 microns in thickness, a cathode no greater than 100 microns in thickness, an electrolyte no greater than 20 microns in thickness, and an interconnect no greater than 30 microns in thickness.
  • a fuel cell comprises an anode no greater than 50 microns in thickness, a cathode no greater than 50 microns in thickness, an electrolyte no greater than 10 microns in thickness, and an interconnect no greater than 25 microns in thickness.
  • the interconnect has a thickness in the range of from 1 micron to 20 microns.
  • the fuel cell comprises a barrier layer between the anode and the electrolyte, or a barrier layer between the cathode and the electrolyte, or both barrier layers.
  • the barrier layers are the interconnects. In such cases, the reactants are directly injected into the anode and the cathode.
  • the cathode has a thickness of no greater than 15 microns, or no greater than 10 microns, or no greater than 5 microns.
  • the anode has a thickness of no greater than 15 microns, or no greater than 10 microns, or no greater than 5 microns.
  • the electrolyte has a thickness of no greater than 5 microns, or no greater than 2 microns, or no greater than 1 micron, or no greater than 0.5 micron.
  • the interconnect is made of a material comprising metal, stainless steel, silver, metal alloys, nickel, nickel oxide, ceramics, or graphene.
  • the fuel cell has a total thickness of no less than 1 micron.
  • each fuel cell comprises an anode no greater than 25 microns in thickness, a cathode no greater than 25 microns in thickness, an electrolyte no greater than 10 microns in thickness, and an interconnect having a thickness of from 100 nm to 100 microns.
  • each fuel cell comprises a barrier layer between the anode and the electrolyte, or a barrier layer between the cathode and the electrolyte, or both barrier layers.
  • the barrier layers are the interconnects.
  • the interconnect is made of silver.
  • the interconnect has a thickness of from 500 nm to 1000 nm.
  • the interconnect is made of a material comprising metal, stainless steel, silver, metal alloys, nickel, nickel oxide, ceramics, or graphene.
  • the cathode has a thickness of no greater than 15 microns, or no greater than 10 microns, or no greater than 5 microns.
  • the anode has a thickness of no greater than 15 microns, or no greater than 10 microns, or no greater than 5 microns.
  • the electrolyte has a thickness of no greater than 5 microns, or no greater than 2 microns, or no greater than 1 micron, or no greater than 0.5 micron.
  • each fuel cell has a total thickness of no less than 1 micron.
  • steps (a)-(c) are performed using additive manufacturing.
  • said additive manufacturing employs extrusion, photopolymerization, powder bed fusion, material jetting, binder jetting, directed energy deposition, lamination.
  • the method comprises assembling the anode, the cathode, and the electrolyte using additive manufacturing. In an embodiment, the method comprises forming an interconnect and assembling the interconnect with the anode, the cathode, and the electrolyte.
  • the method comprises making at least one barrier layer.
  • said at least one barrier layer is used between the electrolyte and the cathode or between the electrolyte and the anode or both.
  • said at least one barrier layer is also an interconnect.
  • the method comprises heating the fuel cell such that shrinkage rates of the anode, the cathode, and the electrolyte are matched. In an embodiment, such heating takes place for no greater than 30 minutes, preferably no greater than 30 seconds, and most preferably no greater than 30 milliseconds. In this disclosure, matching shrinkage rates during heating is discussed in details below (Matching SRTs).
  • a fuel cell comprises a first composition and a second composition, wherein the first composition has a first shrinkage rate and the second composition has a second shrinkage rate
  • the heating described in this disclosure preferably takes place such that the difference between the first shrinkage rate and the second shrinkage rate is no greater than 75% of the first shrinkage rate.
  • the heating employs electromagnetic radiation (EMR).
  • EMR electromagnetic radiation
  • EMR comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam.
  • heating is performed in situ.
  • Also disclosed herein is a method of making a fuel cell stack comprising a multiplicity of fuel cells, the method comprising (a) forming an anode no greater than 25 microns in thickness in each fuel cell, (b) forming a cathode no greater than 25 microns in thickness in each fuel cell, (c) forming an electrolyte no greater than 10 microns in thickness in each fuel cell, and (d) producing an interconnect having a thickness of from 100 nm to 100 microns in each fuel cell.
  • steps (a)-(d) are performed using additive manufacturing.
  • said additive manufacturing employs extrusion, photopolymerization, powder bed fusion, material jetting, binder jetting, directed energy deposition, and/or lamination.
  • the method comprises assembling the anode, the cathode, the electrolyte, and the interconnect using additive manufacturing. In an embodiment, the method comprises making at least one barrier layer in each fuel cell. In an embodiment, said at least one barrier layer is used between the electrolyte and the cathode or between the electrolyte and the anode or both. In an embodiment, said at least one barrier layer is the interconnect.
  • the method comprises heating each fuel cell such that shrinkage rates of the anode, the cathode, and the electrolyte are matched. In an embodiment, such heating takes place for no greater than 30 minutes, or no greater than 30 seconds, or no greater than 30 milliseconds.
  • said heating comprises electromagnetic radiation (EMR).
  • EMR electromagnetic radiation
  • EMR comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam. In an embodiment, heating is performed in situ.
  • the method comprises heating the entire fuel cell stack such that shrinkage rates of the anode, the cathode, and the electrolyte are matched. In an embodiment, such heating takes place for no greater than 30 minutes, or no greater than 30 seconds, or no greater than 30 milliseconds.
  • the cathode comprises perovskites, such as LSC, LSCF, LSM.
  • the cathode comprises lanthanum, cobalt, strontium, manganite.
  • the cathode is porous.
  • the cathode comprises YSZ, Nitrogen, Nitrogen Boron doped Graphene, Lao.6Sro.4CoO.2FeO.8O3, SrCoo.5Sco.5O3, BaFeo.75TaO.25O3, BaFeo. 875 Reo.i 25 0 3 , Bao. 5 Lao.i 25 Zno. 375 Ni0 3 , Bao. 75 Sr0.25Feo. 875 Gao.i 25 0 3 , BaFeo.125Coo.125, Zro.7503.
  • the cathode comprises LSCo, LCo, LSF, LSCoF. In an embodiment, the cathode comprises perovskites LaCo0 3 , LaFe0 3 , LaMn0 3 , (La,Sr)Mn0 3 , LSM-GDC, LSCF-GDC, LSC-GDC. Cathodes containing LSCF are suitable for intermediate-temperature fuel cell operation.
  • the cathode comprises a material selected from the group consisting of lanthanum strontium manganite, lanthanum strontium ferrite, and lanthanum strontium cobalt ferrite. In an embodiment, the cathode comprises lanthanum strontium manganite.
  • the anode comprises Copper, Nickle-Oxide, Nickle-Oxide-YSZ, NiO- GDC, NiO-SDC, Aluminum doped Zinc Oxide, Molybdenum Oxide, Lanthanum, strontium, chromite, ceria, perovskites (such as, LSCF [La ⁇ l-x ⁇ Sr ⁇ x ⁇ Co ⁇ l-y ⁇ Fe ⁇ y ⁇ 0 3 ] or LSM [La ⁇ l- x ⁇ Sr ⁇ x ⁇ Mn03], where x is usually 0.15-0.2 and y is 0.7 to 0.8).
  • the anode comprises SDC or BZCYYb coating or barrier layer to reduce coking and sulfur poisoning.
  • the anode is porous.
  • the anode comprises combination of electrolyte material and electrochemically active material, combination of electrolyte material and electrically conductive material.
  • the anode comprises nickel and yttria stabilized zirconia. In an embodiment, the anode is formed by reduction of a material comprising nickel oxide and yttria stabilized zirconia. In an embodiment, the anode comprises nickel and gadolinium stabilized ceria. In an embodiment, the anode is formed by reduction of a material comprising nickel oxide and gadolinium stabilized ceria. Electrolyte
  • the electrolyte in a fuel cell comprises stabilized zirconia e.g., YSZ, YSZ-8, Y0.16Zr0.84O 2 .
  • the electrolyte comprises doped LaGa0 3 , e.g., LSGM, Lao. 9 SrO.lGaO.8MgO.2O 3 .
  • the electrolyte comprises doped ceria, e.g., GDC, Gdo. 2 Ceo. 8 O 2 .
  • the electrolyte comprises stabilized bismuth oxide e.g., BVCO, Bi2Vo. 9 CuO.105.35.
  • the electrolyte comprises zirconium oxide, yttria stabilized zirconium oxide (also known as YSZ, YSZ8 (8mole% YSZ)), ceria, gadolinia, scandia, magnesia, calcia.
  • the electrolyte is sufficiently impermeable to prevent significant gas transport and prevent significant electrical conduction; and allow ion conductivity.
  • the electrolyte comprises doped oxide such as cerium oxide, yttrium oxide, bismuth oxide, lead oxide, lanthanum oxide.
  • the electrolyte comprises perovskite, such as, LaCoFe0 3 or LaCo0 3 or Ceo. 9 Gdo. 1 O 2 (GDC) or Ceo. 9 Smo. 1 O 2 (SDC, samaria doped ceria) or scandia stabilized zirconia.
  • the electrolyte comprises a material selected from the group consisting of zirconia, ceria, and gallia.
  • the material is stabilized with a stabilizing material selected from the group consisting of scandium, samarium, gadolinium, and yttrium.
  • the material comprises yttria stabilized zirconia.
  • an electrolyte comprising (a) formulating a colloidal suspension, wherein the colloidal suspension comprises an additive, particles having a range of diameters and a size distribution, and a solvent; (b) forming an electrolyte comprising the colloidal suspension; and (c) heating at least a portion of the electrolyte; wherein formulating the colloidal suspension is preferably optimized by controlling the pH of the colloidal suspension, or concentration of the binder in the colloidal suspension, or composition of the binder in the colloidal suspension, or the range of diameters of the particles, or maximum diameter of the particles, or median diameter of the particles, or the size distribution of the particles, or boiling point of the solvent, or surface tension of the solvent, or composition of the solvent, or thickness of the minimum dimension of the electrolyte, or the composition of the particles, or combinations thereof.
  • a method of making a fuel cell comprising (a) obtaining a cathode and an anode; (b) modifying the cathode surface and the anode surface; (c) formulating a colloidal suspension, wherein the colloidal suspension comprises an additive, particles having a range of diameters and a size distribution, and a solvent; (d) forming an electrolyte comprising the colloidal suspension between the modified anode surface and the modified cathode surface; and (e) heating at least a portion of the electrolyte; wherein formulating the colloidal suspension comprises controlling pH of the colloidal suspension, or concentration of the binder in the colloidal suspension, or composition of the binder in the colloidal suspension, or the range of diameters of the particles, or maximum diameter of the particles, or median diameter of the particles, or the size distribution of the particles, or boiling point of the solvent, or surface tension of the solvent, or composition of the solvent, or thickness of the minimum dimension of the electrolyte, or the composition of the particles,
  • the anode and the cathode are obtained via any suitable means.
  • the modified anode surface and the modified cathode surface have a maximum height profile roughness that is less than the average diameter of the particles in the colloidal suspension.
  • the maximum height profile roughness refers to the maximum distance between any trough and an adjacent peak as illustrated in Figure 9.
  • the anode surface and the cathode surface are modified via any suitable means.
  • a method of making a fuel cell comprising (a) obtaining a cathode and an anode; (b) formulating a colloidal suspension, wherein the colloidal suspension comprises an additive, particles having a range of diameters and a size distribution, and a solvent; (c) forming an electrolyte comprising the colloidal suspension between the anode and the cathode; and (d) heating at least a portion of the electrolyte; wherein formulating the colloidal suspension comprises controlling pH of the colloidal suspension, or concentration of the binder in the colloidal suspension, or composition of the binder in the colloidal suspension, or the range of diameters of the particles, or maximum diameter of the particles, or median diameter of the particles, or the size distribution of the particles, or boiling point of the solvent, or surface tension of the solvent, or composition of the solvent, or thickness of the minimum dimension of the electrolyte, or the composition of the particles, or combinations thereof.
  • the anode and the cathode are obtained via any suitable means.
  • the anode surface in contact with the electrolyte and the cathode surface in contact with the electrolyte have a maximum height profile roughness that is less than the average diameter of the particles in the colloidal suspension.
  • the solvent comprises water. In an embodiment, the solvent comprises an organic component. In an embodiment, the solvent comprises ethanol, butanol, alcohol, terpineol, Diethyl ether 1,2-Dimethoxyethane (DME (ethylene glycol dimethyl ether), 1- Propanol (n-propanol, n-propyl alcohol), or butyl alcohol. In an embodiment, the solvent surface tension is less than half of water's surface tension in air. In an embodiment, the solvent surface tension is less than 30 mN/m at atmospheric conditions.
  • DME Diethyl ether 1,2-Dimethoxyethane
  • DME ethylene glycol dimethyl ether
  • 1- Propanol n-propanol, n-propyl alcohol
  • the solvent surface tension is less than half of water's surface tension in air. In an embodiment, the solvent surface tension is less than 30 mN/m at atmospheric conditions.
  • the electrolyte is formed adjacent to a first substrate. In an embodiment, the electrolyte is formed between a first substrate and a second substrate. In an embodiment, the first substrate has a maximum height profile roughness that is less than the average diameter of the particles. In an embodiment, the particles have a packing density greater than 40%, or greater than 50%, or greater than 60%. In an embodiment, the particles have a packing density close to the random close packing (RCP) density.
  • RCP random close packing
  • Random close packing is an empirical parameter used to characterize the maximum volume fraction of solid objects obtained when they are packed randomly.
  • a container is randomly filled with objects, and then the container is shaken or tapped until the objects do not compact any further, at this point the packing state is RCP.
  • the packing fraction is the volume taken by number of particles in a given space of volume.
  • the packing fraction determines the packing density. For example, when a solid container is filled with grain, shaking the container will reduce the volume taken up by the objects, thus allowing more grain to be added to the container. Shaking increases the density of packed objects. When shaking no longer increases the packing density, a limit is reached and if this limit is reached without obvious packing into a regular crystal lattice, this is the empirical random close-packed density.
  • the median particle diameter is between 50 nm and 1000 nm, or between 100 nm and 500 nm, or approximately 200 nm.
  • the first substrate comprises particles having a median particle diameter, wherein the median particle diameter of the electrolyte is no greater than 10 times and no less than 1/10 of the median particle diameter of the first substrate.
  • the first substrate comprises a particle size distribution that is bimodal having a first mode and a second mode, each having a median particle diameter.
  • the median particle diameter in the first mode of the first substrate is greater than 2 times, or greater than 5 times, or greater than 10 times that of the second mode.
  • the particle size distribution of the first substrate is adjusted to change the behavior of the first substrate during heating.
  • the first substrate has a shrinkage that is a function of heating temperature.
  • the particles in the colloidal suspension has a maximum particle diameter and a minimum particle diameter, wherein the maximum particle diameter is less than 2 times, or less than 3 times, or less than 5 times, or less than 10 times the minimum particle diameter.
  • the minimum dimension of the electrolyte is less than 10 microns, or less than 2 microns, or less than 1 micron, or less than 500 nm.
  • the electrolyte has a gas permeability of no greater than 1 millidarcy, preferably no greater than 100 microdarcy, and most preferably no greater than 1 microdarcy. Preferably, the electrolyte has no cracks penetrating through the minimum dimension of the electrolyte.
  • the boiling point of the solvent is no less than 200 °C, or no less than 100 °C, or no less than 75°C. In an embodiment, the boiling point of the solvent is no greater than 125 °C, or no greater than 100 °C, or no greater than 85 °C, no greater than 70 °C.
  • the pH of the colloidal suspension is no less than 7, or no less than 9, or no less than 10.
  • the additive comprises polyethylene glycol (PEG), ethyl cellulose, polyvinylpyrrolidone (PVP), polyvinyl butyral (PVB), butyl benzyl phthalate (BBP), polyalkalyne glycol (PAG).
  • the additive concentration is no greater than 100 mg/cm3, or no greater than 50 mg/cm3, or no greater than 30 mg/cm3, or no greater than 25 mg/cm3.
  • the colloidal suspension is milled. In an embodiment, the colloidal suspension is milled using a rotational mill. In an embodiment, the rotational mill is operated at no less than 20 rpm, or no less than 50 rpm, or no less than 100 rpm, or no less than 150 rpm.
  • the colloidal suspension is milled using zirconia milling balls or tungsten carbide balls. In an embodiment, the colloidal suspension is milled for no less than 2 hours, or no less than 4 hours, or no less than 1 day, or no less than 10 days.
  • the particle concentration in the colloidal suspension is no greater than 30 wt%, or no greater than 20 wt%, or no greater than 10 wt%. In an embodiment, the particle concentration in the colloidal suspension is no less than 2 wt%. In an embodiment, the particle concentration in the colloidal suspension is no greater than 10 vol%, or no greater than 5 vol%, or no greater than 3 vol%, or no greater than 1 vol%. In an embodiment, the particle concentration in the colloidal suspension is no less than 0.1 vol%.
  • the electrolyte is formed using an additive manufacturing machine (AMM).
  • the first substrate is formed using an AMM.
  • said heating comprises the use of electromagnetic radiation (EMR).
  • EMR electromagnetic radiation
  • the EMR comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser.
  • the first substrate and the electrolyte are heated to cause co sintering.
  • the first substrate, the second substrate, and the electrolyte are heated to cause co-sintering.
  • the EMR is controlled to preferentially sinter the first substrate over the electrolyte.
  • the electrolyte is in compression throughout its thickness after heating.
  • the first substrate and the second substrate apply compressive stress to the electrolyte after heating.
  • the first substrate and the second substrate are anode and cathode of a fuel cell.
  • the minimum dimension of the electrolyte is between 500 nm and 5 microns. In an embodiment, the minimum dimension of the electrolyte is between 1 micron and 2 microns.
  • the interconnect comprises silver, gold, platinum, AISI441, ferritic stainless steel, stainless steel, Lanthanum, Chromium, Chromium Oxide, Chromite, Cobalt, Cesium, Cr 2 0 3 .
  • the anode comprises LaCr0 3 (lanthanum chromite) coating on Cr 2 0 3 or NiC0 2 0 4 or MnC0 2 0 4 coatings.
  • the interconnect surface is coated with Cobalt and/or Cesium.
  • the interconnect comprises ceramics.
  • the interconnect comprises Lanthanum Chromite or doped Lanthanum Chromite.
  • the interconnect is made of a material comprising metal, stainless steel, ferritic steel, crofer, lanthanum chromite, silver, metal alloys, nickel, nickel oxide, ceramics, or graphene.
  • the fuel cell comprises a catalyst, such as, platinum, palladium, scandia, chromium, cobalt, cesium, Ce0 2 , nickle, nickle oxide, zine, copper, titantia, ruthenium, rhodiu, MoS 2 , molybdenum, rhenium, vandia, manganese, magnesium, iron.
  • the catalyst promotes methane reforming reactions to generate hydrogen and carbon monoxide for them to be oxidized in the fuel cell.
  • the catalyst is part of the anode, especially nickel anode has inherent methane reforming properties.
  • the catalyst is between l%-5%, or 0.1% to 10% by mass.
  • the catalyst is used on the anode surface or in the anode.
  • such anode catalysts reduce harmful coking reactions and carbon deposits.
  • simple oxide version of catalysts is used or perovskite.
  • 2% mass Ce0 2 catalyst is used for methane-powered fuel cells.
  • the catalyst is dipped or coated on the anode.
  • the catalyst is made by an additive manufacturing machine (AMM) and incorporated into the fuel cell using the AMM.
  • AMM additive manufacturing machine
  • the fuel cell stack is configured to be made into a cartridge form, such as an easily detachable flanged fuel cell cartridge (FCC) design.
  • FCC fuel cell cartridge
  • 1111 represents holes for bolts
  • 1112 represents a cathode in the FCC
  • 1113 represents an electrolyte in the FCC
  • 1114 represents an anode in the FCC
  • 1115 represents gas channels in the electrodes (anode and cathode)
  • 1116 represents an integrated multi-fluid heat exchanger in the FCC.
  • Figure 11C illustrates the top view and bottom view of an embodiment of a FCC, in which the length of the oxidant side of the FCC is shown LO, the length of the fuel side of the FCC is shown L f , the width of the oxidant (air) entrance is shown WO, the width of the fuel entrance is shown W f .
  • two fluid exits are shown (Air Outlet 1132 and Fuel Outlet 1134). In some cases, the anode exhaust and the cathode exhaust are mixed and extracted through one fluid exit.
  • Figure 11B illustrates cross-sectional views of the FCC, wherein air flow is sealed from the anode and fuel flow is sealed from the cathode. The bolts are isolated electrically with a seal as well.
  • the seal is a dual functional seal (DFS) comprising YSZ (yttria-stabilized zirconia) or a mixture of 3YSZ (3 mol% Y2O3 in ZrCh) and 8YSZ (8 mol% Y2O3 in ZrCh).
  • DFS dual functional seal
  • the DFS is impermeable to non-ionic substances and electrically insulating.
  • the mass ratio of 3YSZ/8YSZ is in the range of from 10/90 to 90/10.
  • the mass ratio of 3YSZ/8YSZ is about 50/50.
  • the mass ratio of 3YSZ/8YSZ is 100/0 or 0/100.
  • a fuel cell cartridge comprising an anode, a cathode, an electrolyte, an interconnect, a fuel entrance on a fuel side of the FCC, an oxidant entrance on an oxidant side of the FCC, at least one fluid exit, wherein the fuel entrance has a width of W f , the fuel side of the FCC has a length of L f , the oxidant entrance has a width of WO, the oxidant side of the FCC has a length of LO, wherein W f /L f is in the range of 0.1 to 1.0, or 0.1 to 0.9, or 0.2 to 0.9, or 0.5 to 0.9, or 0.5 to 1.0 and WO/LO is in the range of 0.1 to 1.0, or 0.1 to 0.9, or 0.2 to 0.9, or 0.5 to 0.9, or 0.5 to 1.0.
  • W f /L f is in the range of 0.1 to 1.0, or 0.1 to 0.9, or 0.2 to 0.9,
  • said entrances and exit are on one surface of the FCC and said FCC comprises no protruding fluid passage on said surface.
  • said surface is smooth with a maximum elevation change of no greater than 1 mm, or no greater than 100 microns, or no greater than 10 microns.
  • the FCC comprises a barrier layer between the electrolyte and the cathode or between the electrolyte and the anode or both.
  • the FCC comprises dual functional seal that is impermeable to non-ionic substances and electrically insulating.
  • said dual functional seal comprises YSZ (yttria-stabilized zirconia) or a mixture of 3YSZ (3 mol% Y2O3 in ZrCh) and 8YSZ (8 mol% Y2O3 in ZrCh).
  • said interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid dispersing components.
  • said anode and cathode comprise fluid dispersing components.
  • interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid channels.
  • the FCC is detachably fixed to a mating surface and not soldered nor welded to said mating surface.
  • the FCC is bolted to or pressed to said mating surface.
  • said mating surface comprises matching fuel entrance, matching oxidant entrance, and at least one matching fluid exit.
  • a fuel cell cartridge comprising an anode, a cathode, an electrolyte, an interconnect, a fuel entrance, an oxidant entrance, at least one fluid exit, wherein said entrances and exit are on one surface of the FCC and said FCC comprises no protruding fluid passage on said surface.
  • said surface is smooth with a maximum elevation change of no greater than 1 mm, or no greater than 100 microns, or no greater than 10 microns.
  • the FCC comprises dual functional seal that is impermeable to non ionic substances and electrically insulating.
  • said interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid dispersing components.
  • said interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid channels.
  • the FCC is detachably fixed to a mating surface and not soldered nor welded to said mating surface.
  • the FCC is bolted to or pressed to said mating surface.
  • said mating surface comprises matching fuel entrance, matching oxidant entrance, and at least one matching fluid exit.
  • an assembly comprising a fuel cell cartridge (FCC) and a mating surface, wherein the FCC comprises an anode, a cathode, an electrolyte, an
  • a fuel entrance on a fuel side of the FCC an oxidant entrance on an oxidant side of the FCC, at least one fluid exit
  • the fuel entrance has a width of W f
  • the fuel side of the FCC has a length of L f
  • the oxidant entrance has a width of WO
  • the oxidant side of the FCC has a length of LO
  • W f /L f is in the range of 0.1 to 1.0, or 0.1 to 0.9, or 0.2 to 0.9, or 0.5 to 0.9, or 0.5 to 1.0
  • WO/LO is in the range of 0.1 to 1.0, or 0.1 to 0.9, or 0.2 to 0.9, or 0.5 to 0.9, or 0.5 to 1.0, wherein the FCC is detachably fixed to the mating surface.
  • the FCC is not soldered nor welded to said mating surface. In an embodiment, the FCC is bolted to or pressed to said mating surface. In an embodiment, said mating surface comprises matching fuel entrance, matching oxidant entrance, and at least one matching fluid exit.
  • said entrances and exit are on one surface of the FCC and said FCC comprises no protruding fluid passage on said surface.
  • said surface is smooth with a maximum elevation change of no greater than 1 mm, or no greater than 100 microns, or no greater than 10 microns.
  • said interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid dispersing components.
  • said anode and cathode comprise fluid dispersing components.
  • interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid channels.
  • a method comprising pressing or bolting together a fuel cell cartridge (FCC) and a mating surface, said method excluding welding or soldering together the FCC and the mating surface, wherein the FCC comprises an anode, a cathode, an electrolyte, an interconnect, a fuel entrance on a fuel side of the FCC, an oxidant entrance on an oxidant side of the FCC, at least one fluid exit, wherein the fuel entrance has a width of W f , the fuel side of the FCC has a length of L f , the oxidant entrance has a width of WO, the oxidant side of the FCC has a length of LO, wherein W f /L f is in the range of 0.1 to 1.0, or 0.1 to 0.9, or 0.2 to 0.9, or 0.5 to 0.9, or 0.5 to 1.0 and WO/LO is in the range of 0.1 to 1.0, or 0.1 to 0.9, or 0.2 to
  • said entrances and exit are on one surface of the FCC and said FCC comprises no protruding fluid passage on said surface.
  • said surface is smooth with a maximum elevation change of no greater than 1 mm, or no greater than 100 microns, or no greater than 10 microns.
  • said interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid dispersing components.
  • said interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid channels.
  • a fuel cell cartridge comprising a fuel cell and a fuel cell casing, wherein the fuel cell comprises an anode, a cathode, and an electrolyte, wherein at least a portion of the fuel cell casing is made of the same material as the electrolyte.
  • the electrolyte is in contact with the portion of the fuel cell casing made of the same material.
  • the electrolyte and the portion of the fuel cell casing are made of a dual functional seal (DFS), wherein the DFS comprises 3YSZ (3 mol% Y2O3 in ZrCh) and 8YSZ (8 mol% Y2O3 in ZrCh), wherein the mass ratio of 3YSZ/8YSZ is in the range of from 100/0 to 0/100 or from 10/90 to 90/10 and wherein the DFS is impermeable to non-ionic substances and electrically insulating.
  • the mass ratio of 3YSZ/8YSZ is about 50/50 or 40/60 or 60/40 or 30/70 or 70/30 or 20/80 or 80/20.
  • said fuel cell casing comprises a fuel entrance and fuel passage for the anode, an oxidant entrance and oxidant passage for the cathode, and at least one fluid exit.
  • said entrances and exit are on one surface of the FCC and said FCC comprises no protruding fluid passage on said surface.
  • the fuel cell casing is in contact with at least a portion of the anode.
  • the FCC comprises a barrier layer between the electrolyte and the cathode and between the fuel cell casing and the cathode.
  • the FCC comprises an interconnect, wherein the interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid dispersing components.
  • the FCC comprises an interconnect, wherein the interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid channels.
  • the FCC is detachably fixed to a mating surface and not soldered nor welded to said mating surface.
  • said mating surface comprises matching fuel entrance, matching oxidant entrance, and at least one matching fluid exit.
  • a dual functional seal comprising 3YSZ (3 mol% Y2O3 in ZrCh) and 8YSZ (8 mol% Y2O3 in ZrCh), wherein the mass ratio of 3YSZ/8YSZ is in the range of from 10/90 to 90/10 and wherein the DFS is impermeable to non-ionic substances and electrically insulating.
  • the mass ratio of 3YSZ/8YSZ is about 50/50 or 40/60 or 60/40 or 30/70 or 70/30 or 20/80 or 80/20.
  • the DFS is used as an electrolyte in a fuel cell or as a portion of a fuel cell casing or both.
  • a method comprising providing a dual functional seal (DFS) in a fuel cell system, wherein the DFS comprises 3YSZ (3 mol% Y 2 0 3 in Zr0 2 ) and 8YSZ (8 mol%
  • the mass ratio of 3YSZ/8YSZ is in the range of from 100/0 to 0/100 or from 10/90 to 90/10 and wherein the DFS is impermeable to non-ionic substances and electrically insulating.
  • the mass ratio of 3YSZ/8YSZ is about 50/50 or 40/60 or 60/40 or 30/70 or 70/30 or 20/80 or 80/20.
  • the DFS is used as electrolyte or a portion of a fuel cell casing or both in the fuel cell system.
  • said portion of a fuel cell casing is the entire fuel cell casing.
  • said portion of a fuel cell casing is a coating on the fuel cell casing.
  • the electrolyte and said portion of a fuel cell casing are in contact.
  • a fuel cell system comprising an anode having six surfaces, a cathode having six surfaces, an electrolyte, and an anode surround in contact with at least three surfaces of the anode, wherein the electrolyte is part of the anode surround and said anode surround is made of the same material as the electrolyte.
  • said same material is a dual functional seal (DFS) comprising 3YSZ (3 mol% Y2O3 in ZrCh) and 8YSZ (8 mol% Y2O3 in ZrCh), wherein the mass ratio of 3YSZ/8YSZ is in the range of from 100/0 to 0/100 or from 10/90 to 90/10 and wherein the DFS is impermeable to non-ionic substances and electrically insulating.
  • the mass ratio of 3YSZ/8YSZ is about 50/50 or 40/60 or 60/40 or 30/70 or 70/30 or 20/80 or 80/20.
  • the anode surround is in contact with five surfaces of the anode.
  • the fuel cell system comprises a barrier layer between the cathode and a cathode surround, wherein the barrier layer is in contact with at least three surfaces of the cathode, wherein the electrolyte is part of the cathode surround and said cathode surround is made of the same material as the electrolyte.
  • the fuel cell system comprises fuel passage and oxidant passage in the anode surround and the cathode surround.
  • the fuel cell system comprises an interconnect, wherein the interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid dispersing components.
  • the fuel cell system comprises an interconnect, wherein the interconnect comprises no fluid dispersing element and said anode and cathode comprise fluid channels.
  • a device comprising a first electrode 1010, 1011, a second electrode 1020, 1021, and an electrolyte 1030, 1031 between the electrodes, wherein the first electrode 1010, 1011 is configured to receive a fuel and no oxygen 1040, wherein the second electrode 1020, 1021 is configured to receive water or nothing 1050, wherein the device is configured to simultaneously produce hydrogen 1070 from the second electrode and syngas 1060 from the first electrode.
  • 1040 represents methane and water or methane and carbon dioxide.
  • 1030 represents an oxide ion conducting membrane.
  • 1031 represents a proton conducting membrane
  • 1011 and 1021 represent Ni-barium zirconate electrodes.
  • 1010 and 1020 represent Ni-YSZ or NiO-YSZ electrodes
  • 1040 represents hydrocarbon and water or hydrocarbon and carbon dioxide
  • 1050 represents water or water and hydrogen.
  • 1010 represents Cu-CGO electrode optionally with CuO or CU2O or combinations thereof
  • 1020 represents Ni-YSZ or NiO-YSZ electrode
  • 1040 represents hydrocarbon with little to no water, with no carbon dioxide, and with no oxygen
  • 1050 represents water or water and hydrogen.
  • no oxygen means there is no oxygen present at the first electrode or at least not enough oxygen that would interfere with the reaction.
  • water only means that the intended feedstock is water and does not exclude trace elements or inherent components in water.
  • water containing salts or ions is considered to be within the scope of water only.
  • Water only also does not require 100% pure water but includes this embodiment.
  • the hydrogen produced from the second electrode is pure hydrogen, which means that in the produced gas phase from the second electrode, hydrogen is the main component.
  • the hydrogen content is no less than 99.5%.
  • the hydrogen content is no less than 99.9%.
  • the hydrogen produced from the second electrode is the same purity as that produced from electrolysis of water.
  • said first electrode is configured to receive methane and water or methane and carbon dioxide.
  • said fuel comprises a hydrocarbon having a carbon number in the range of 1-12 or 1-10 or 1-8. Most preferably, the fuel is methane or natural gas, which is predominantly methane.
  • the device does not generate electricity.
  • the device comprises a mixer configured to receive at least a portion of the first electrode product and at least a portion of the second electrode product. In an embodiment, said mixer is configured to generate a gas stream in which the hydrogen to carbon oxides ratio is no less than 2 or no less than 3 or between 2 and 3.
  • said first electrode or second electrode or both comprise a catalyst and a substrate, wherein the mass ratio between the catalyst and the substrate is in no less than 1/100 or no less than 1/10 or no less than 1/5, or no less than 1/3, or no less than 1/1.
  • the catalyst comprises nickel oxide, silver, cobalt, cesium, nickel, iron, manganese, nitrogen, tetra-nitrogen, molybdenum, copper, chromium, rhodium, ruthenium, palladium, osmium, iridium, platinum, or combinations thereof.
  • the substrate comprises gadolinium, CeC> 2 , ZrC> 2 , S1O 2 , T1O 2 , steel, cordierite (2Mg0-2AI20 3 -5Si0 2 ), aluminum titanate (AI2T ⁇ 05), silicon carbide (SiC), all phases of aluminum oxide, yttria or scandia-stabilized zirconia (YSZ), gadolinia or samaria-doped ceria, or combinations thereof.
  • said first electrode or second electrode or both comprise a promoter.
  • said promoter comprises Mo, W, Ba, K, Mg, Fe, or combinations thereof.
  • said electrodes and electrolyte form a repeat unit and said device comprises multiple repeat units separated by interconnects.
  • the interconnects comprise no fluid dispersing element.
  • said first electrode or second electrode or both comprise fluid channels or alternatively said first electrode or second electrode or both comprise fluid dispersing components.
  • a method comprising forming a first electrode, forming a second electrode, and forming an electrolyte between the electrodes, wherein the electrodes and electrolyte are assembled as they are formed, wherein the first electrode is configured to receive a fuel and no oxygen, wherein the second electrode is configured to receive water only or nothing, wherein the device is configured to simultaneously produce hydrogen from the second electrode and syngas from the first electrode.
  • said forming comprises material jetting, binder jetting, inkjet printing, aerosol jetting, or aerosol jet printing, vat photopolymerization, powder bed fusion, material extrusion, directed energy deposition, sheet lamination, ultrasonic inkjet printing, or combinations thereof.
  • said electrodes and electrolyte form a repeat unit and said method comprises forming said multiple repeat units and forming interconnects between the repeat units.
  • the method comprises forming fluid channels or fluid dispersing components in the first electrode or the second electrode or both.
  • the method comprises heating in situ.
  • said heating comprises electromagnetic radiation (EMR).
  • EMR comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam.
  • a method comprising providing a device comprising a first electrode, a second electrode, and an electrolyte between the electrodes, introducing a fuel without oxygen to the first electrode, introducing water only or nothing to the second electrode to generate hydrogen, extracting hydrogen from the second electrode, and extracting syngas from the first electrode.
  • the fuel comprises methane and water or methane and carbon dioxide.
  • said fuel comprises a hydrocarbon having a carbon number in the range of 1-12 or 1-10 or 1-8.
  • the method comprises feeding at least a portion of the extracted syngas to a Fischer-Tropsch reactor. In an embodiment, the method comprises feeding at least a portion of the extracted hydrogen to the Fischer-Tropsch reactor. In an embodiment, said at least portion of the extracted syngas and said at least portion of the extracted hydrogen are adjusted such that the hydrogen to carbon oxides ratio is no less than 2 or no less than 3 or between 2 and 3.
  • the fuel is directly introduced into the first electrode or water is directly introduced into the second electrode or both.
  • said first electrode or second electrode or both comprise a catalyst and a substrate, wherein the mass ratio between the catalyst and the substrate is in no less than 1/100 or no less than 1/10 or no less than 1/5, or no less than 1/3, or no less than 1/1.
  • the catalyst comprises nickel oxide, silver, cobalt, cesium, nickel, iron, manganese, nitrogen, tetra-nitrogen, molybdenum, copper, chromium, rhodium, ruthenium, palladium, osmium, iridium, platinum, or combinations thereof.
  • the substrate comprises gadolinium, CeC>2, ZrC>2, SiC>2, T1O2, steel, cordierite (2MgO-2Al 2 C> 3 -5SiC> 2 ), aluminum titanate (AI2T ⁇ 05), silicon carbide (SiC), all phases of aluminum oxide, yttria or scandia-stabilized zirconia (YSZ), gadolinia or samaria-doped ceria, or combinations thereof.
  • the method comprises applying a potential difference between the electrodes.
  • the method comprises using the extracted hydrogen in one of the following or combinations thereof: Fischer-Tropsch (FT) reaction; Dry reforming
  • the gas producer is not a fuel cell and does not generate electricity, in various embodiments. Electricity may be applied to the gas producer at the anode and cathode in some cases. In other cases, electricity is not needed.
  • Both the cathode and the anode are electrodes in the electrochemical gas producer. Examples of anode and cathode material are discussed below. In an operating device, the actual anode and cathode designation depends on where reduction and oxidation reactions take place. In certain embodiments, a material acts as an anode with a set of operating conditions and/or feedstocks and the same material acts as a cathode with a different set of operating conditions and/or feedstocks. As such, the listing of material under anode or cathode is not limiting. Furthermore, the listings of anode/cathode materials apply to the first electrode and second electrode as discussed above.
  • the cathode comprises perovskites, such as LSC, LSCF, LSM.
  • the cathode comprises lanthanum, cobalt, strontium, manganite.
  • the cathode is porous.
  • the cathode comprises YSZ, Nitrogen, Nitrogen Boron doped Graphene, Lao. 6 Sro. 4 CoO.2FeO.8O 3 , SrCoo. 5 Sco. 5 O 3 , BaFeo.
  • the cathode comprises LSCo, LCo, LSF, LSCoF.
  • the cathode comprises perovskites LaCo0 3 , LaFe0 3 , LaMn0 3 , (La,Sr)Mn0 3 , LSM-GDC, LSCF-GDC, LSC-GDC.
  • Cathodes containing LSCF are suitable for intermediate-temperature electrochemical gas producer operation.
  • the cathode comprises Cu-CGO, CuO-CGO, CU 2 O- CGO, or combinations thereof.
  • the cathode comprises a material selected from the group consisting of lanthanum strontium manganite, lanthanum strontium ferrite, and lanthanum strontium cobalt ferrite. In an embodiment, the cathode comprises lanthanum strontium manganite. [213] In an embodiment, the cathode comprises Ba(Ceo. 4 Pro. 4 Yo. 2 )C> 3 ; PrBaCuFeOs; BaCeo. 5 Bio. 5 O 3 ; SmBaC0 2 0 5 ; BaCeo. 5 Feo. 5 O 3 ; GdBaC0 2 0s; SmBao. 5 Sro. 5 C0 2 0s; PrBaC0 2 0s; or combinations thereof. In an embodiment, the cathode is a composite comprising
  • Bao. 5 Sro. 5 Coo. 5 Feo. 5 O 3 and BZCY (for example in a weight ratio of 3:2), wherein BZCY is
  • the cathode is a composite comprising Smo.sSro.sCoOs and Ceo. 8 Smo. 2 O 2 (for example in a weight ratio of 6:4).
  • the cathode is a composite comprising Smo.sSro.sCoOs and BZCY (for example in a weight ratio of 7:3).
  • the anode comprises Nickle-Oxide, Nickle-Oxide-YSZ, NiO-GDC, NiO- SDC, Aluminum doped Zinc Oxide, Molybdenum Oxide, Lanthanum, strontium, chromite, ceria, perovskites (such as, LSCF [La ⁇ l-x ⁇ Sr ⁇ x ⁇ Co ⁇ l-y ⁇ Fe ⁇ y ⁇ 0 3 ] or LSM [La ⁇ l-x ⁇ Sr ⁇ x ⁇ Mn0 3 ], where x is usually 0.15-0.2 and y is 0.7 to 0.8).
  • the anode comprises SDC or BZCYYb coating or barrier layer to reduce coking and sulfur poisoning.
  • the anode is porous.
  • the anode comprises combination of electrolyte material and electrochemically active material, combination of electrolyte material and electrically conductive material.
  • the anode comprises nickel and yttria stabilized zirconia. In an embodiment, the anode is formed by reduction of a material comprising nickel oxide and yttria stabilized zirconia. In an embodiment, the anode comprises nickel and gadolinium stabilized ceria. In an embodiment, the anode is formed by reduction of a material comprising nickel oxide and gadolinium stabilized ceria.
  • the anode comprises NiO. In an embodiment, the anode comprises NiO-BZCY (1:1) and pore former. In an embodiment, the anode comprises NiO-BZCY (6:4) and corn starch. In an embodiment, the anode comprises NiO-BZCY (6:4) and starch/NiO-BZCY (6:4). In an embodiment, the anode comprises NiO-BZCY (6:4). In an embodiment, the anode comprises NiO-BZCY. In an embodiment, the anode comprises NiO-BZCY (6:4) and starch/NiO- BZCY (1:1). In an embodiment, the anode comprises Cu-CGO, CuO-CGO, Cu 2 0-CGO, or combinations thereof. Electrochemical (EC) Compressor
  • an electrochemical compressor comprising an anode, a cathode, an electrolyte between the anode and the cathode, a porous bipolar plate (PBP), an integrated support, a fluid distributor at a first end of the compressor, and a fluid collector at a second end of the compressor, wherein said support is impermeable to non-ionic substances and electrically insulating.
  • the PBP is electrically conductive and permeable to gases (such as H 2 , 0 2 ).
  • an electrochemical compressor comprises a multiplicity of such repeat units between the fluid distributor 1085 and the fluid collector 1086.
  • the electrochemical compressor is configured to provide between the first end and the second end of the compressor a fluid pressure differential no less than 4000 psi, or no less than 5000 psi, or no less than 6000 psi, or no less than 7000 psi, or no less than 8000 psi, or no less than 9000 psi, or no less than lOOOOpsi.
  • said support is part of the electrolyte, or the anode, or the cathode, or the PBP, or combinations thereof.
  • said support has a lattice structure that is regular or irregular.
  • the anode or cathode or both comprise fluid channels or alternatively the anode or cathode or both comprise fluid dispersing components.
  • an electrochemical compressor comprising depositing an anode, a cathode, an electrolyte between the anode and the cathode, and a porous bipolar plate (PBP) to form said compressor.
  • the method comprises providing a fluid distributor at a first end of the compressor and a fluid collector at a second end of the compressor.
  • said depositing comprises material jetting, binder jetting, inkjet printing, aerosol jetting, or aerosol jet printing, vat photopolymerization, powder bed fusion, material extrusion, directed energy deposition, sheet lamination, ultrasonic inkjet printing, or combinations thereof.
  • the method comprises co-sintering the anode, the cathode, the electrolyte, and the PBP.
  • the method comprises heating in situ.
  • said heating comprises electromagnetic radiation (EMR).
  • EMR comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam.
  • the method comprises depositing an integrated support, wherein said support is impermeable to non-ionic substances and electrically insulating.
  • said support has a lattice structure that is regular or irregular.
  • said support is part of the electrolyte, or the anode, or the cathode, or the PBP, or combinations thereof.
  • the method comprises forming fluid dispersing components or fluid channels in the anode or cathode or both.
  • an electrochemical compressor comprising providing said compressor having an anode, a cathode, an electrolyte between the anode and the cathode, and a porous bipolar plate (PBP), an integrated support, a fluid distributor at a first end of the compressor, and a fluid collector at a second end of the compressor, wherein said support is impermeable to non-ionic substances and electrically insulating.
  • PBP porous bipolar plate
  • said electrochemical compressor provides between the first end and the second end of the compressor a fluid pressure differential no less than 4000 psi, or no less than 5000 psi, or no less than 6000 psi, or no less than 7000 psi, or no less than 8000 psi, or no less than 9000 psi, or no less than lOOOOpsi.
  • said electrochemical compressor increases the pressure of hydrogen or oxygen from the first end to the second end.
  • the method comprises using the compressor for hydrogen storage.
  • the method comprises using the compressor for fueling vehicles. In an embodiment, the method comprises using the compressor in pressurized hydrogen
  • an electrochemical compressor As an example, as illustrated in Figure IOC, all the layers of an electrochemical compressor are formed and assembled via printing.
  • the material for making the anode, the cathode, the electrolyte, the PBP, and the integrated support, respectively, is made into an ink form comprising a solvent and particles (e.g., nanoparticles).
  • the ink optionally comprises a dispersant, a binder, a plasticizer, a surfactant, a co-solvent, or combinations thereof.
  • NiO and YSZ particles are mixed with a solvent, wherein the solvent is water (e.g., de-ionized water) or an alcohol (e.g., butanol) or a mixture of alcohols. Organic solvents other than alcohols may also be used.
  • a solvent e.g., de-ionized water
  • an alcohol e.g., butanol
  • Organic solvents other than alcohols may also be used.
  • YSZ particles were mixed with a solvent, wherein the solvent is water (e.g., de-ionized water) or an alcohol (e.g., butanol) or a mixture of alcohols. Organic solvents other than alcohols may also be used.
  • metallic particles such as, silver nanoparticles
  • the solvent may include water (e.g., de-ionized water), organic solvents (e.g. mono-, di- , or tri-ethylene glycols or higher ethylene glycols, propylene glycol, 1,4-butanediol or ethers of such glycols, thiodiglycol, glycerol and ethers and esters thereof, polyglycerol, mono-, di-, and tri-ethanolamine, propanolamine, N,N-dimethylformamide, dimethyl sulfoxide,
  • water e.g., de-ionized water
  • organic solvents e.g. mono-, di- , or tri-ethylene glycols or higher ethylene glycols, propylene glycol, 1,4-butanediol or ethers of such glycols, thiodiglycol, glycerol and ethers and esters thereof
  • polyglycerol mono-, di-
  • conducting phase in both electrodes comprises LSCF(-CGO) or LSM(-YSZ).
  • the method and system of this disclosure are suitable for making a catalyst or a catalyst composite, such as a Fischer-Tropsch (FT) catalyst or catalyst composite.
  • a Fischer-Tropsch (FT) catalyst composite comprising a catalyst and a substrate, wherein the mass ratio between the catalyst and the substrate is in no less than 1/100 or no less than 1/10 or no less than 1/5, or no less than 1/3, or no less than 1/1.
  • the catalyst comprises Fe, Co, Ni, or Ru.
  • the substrate comprises AI2O3, ZrC>2, SiC>2, T1O2, Ce0 2 , modified AI20 3 , modified Zr0 2 , modified Si0 2 , modified Ti0 2 , modified Ce0 2 , gadolinium, steel, cordierite (2Mg0-2AI203-5SiC>2), aluminum titanate (AI2T ⁇ 05), silicon carbide (SiC), all phases of aluminum oxide, yttria or scandia-stabilized zirconia (YSZ), gadolinia or samaria- doped ceria, or combinations thereof.
  • the catalyst composite comprises a promoter.
  • said promoter comprises noble metals, or metal cations, or combinations thereof.
  • said promoter comprises B, La, Zr, K, Cu, or combinations thereof.
  • the catalyst composite comprises fluid channels or alternatively fluid dispersing components.
  • the FT reactor/system is miniaturized compared to traditional FT reactors/systems.
  • a method comprising depositing a Fischer-Tropsch (FT) catalyst to a substrate to form a FT catalyst composite, wherein said depositing comprises material jetting, binder jetting, inkjet printing, aerosol jetting, or aerosol jet printing, vat
  • FT Fischer-Tropsch
  • the mass ratio between the catalyst and the substrate is in no less than 1/100 or no less than 1/10 or no less than 1/5, or no less than 1/3, or no less than 1/1.
  • the method comprises forming fluid channels or alternatively fluid dispersing components in the catalyst composite.
  • a system comprising a Fischer-Tropsch (FT) reactor containing a FT catalyst composite comprising a catalyst and a substrate, wherein the mass ratio between the catalyst and the substrate is in no less than 1/100 or no less than 1/10 or no less than 1/5, or no less than 1/3, or no less than 1/1.
  • the catalyst comprises Fe, Co, Ni, or Ru.
  • the substrate comprises AI2O3, ZrC>2, SiC>2, T1O2, CeC>2, modified AI2O3, modified ZrC>2, modified S1O2, modified T1O2, modified CeC>2, gadolinium, steel, cordierite (2Mg0-2AI203-5SiC>2), aluminum titanate (AI2T ⁇ 05), silicon carbide (SiC), all phases of aluminum oxide, yttria or scandia-stabilized zirconia (YSZ), gadolinia or samaria- doped ceria, or combinations thereof.
  • the catalyst composite comprises a promoter.
  • a FT catalyst composite is formed via printing.
  • the catalyst and the substrate/support are made into an ink form comprising a solvent and particles (e.g., nanoparticles).
  • the ink optionally comprises a dispersant, a binder, a plasticizer, a surfactant, a co-solvent, or combinations thereof.
  • the ink may be any kind of suspension.
  • the ink may be treated with a mixing process, such as ultrasonication or high shear mixing.
  • an iron ink is in an aqueous environment.
  • an iron ink is in an organic solvent
  • the iron ink may also include a promoter.
  • the substrate/support may be a suspension or ink of alumina, in an aqueous environment or an organic environment.
  • the substrate ink may be treated with a mixing process, such as ultrasonication or high shear mixing.
  • the substrate ink comprises a promoter.
  • the promoter is added as its own ink, in an aqueous environment or an organic environment.
  • the various inks are printed separately and sequentially. In some cases, the various inks are printed separately and simultaneously, for example, through different print heads. In some cases, the various inks are printed in combination as a mixture.
  • an exhaust from the fuel cell comprises hydrogen, carbon dioxide, water, and optionally carbon monoxide.
  • the exhaust is passed over a FT catalyst (e.g., an iron catalyst) to produce synthetic fuels or lubricants.
  • a FT catalyst e.g., an iron catalyst
  • the FT iron catalyst has the property to promote water gas shift reaction or reverse water gas shift reaction.
  • the FT reactions take place at a temperature in the range of 150-350 °C and a pressure in the range of one to several tens of atmospheres (e.g., 15 atm or 10 atm or 5 atm or 1 atm).
  • Additional hydrogen may be added to the exhaust stream to reach a hydrogen to carbon oxides ratio (carbon dioxide and carbon monoxide) of no less than 2 or no less than 3 or between 2 and 3.
  • SRT refers to a component of the strain rate tensor. Matching SRTs is contemplated in both heating and cooling processes. In a fuel cell or an EC gas producer or an EC compressor or a FT catalyst, multiple materials or compositions exist. These different materials or compositions often have different thermal expansion coefficients. As such, the heating or cooling process often causes strain or even cracks in the material. We have unexpectedly discovered a treating process (heating or cooling) to match the SRTs of different materials/compositions to reduce, minimize, or even eliminate undesirable effects.
  • FIG. 7 shows the SRTs of a first composition and a second composition as a function of temperature.
  • the SRTs are measured in mm/min.
  • the difference between the first SRT and the second SRT is no greater than 50% or 30% or 20% of the first SRT.
  • heating is achieved via at least one of the following:
  • heating comprises electromagnetic radiation (EMR).
  • EMR electromagnetic radiation
  • EMR comprises UV light, near ultraviolet light, near infrared light, infrared light, visible light, laser, electron beam.
  • the first composition and the second composition are heated at the same time. In an embodiment, the first composition and the second composition are heated at different times. In an embodiment, the first composition is heated for a first period of time, the second composition is heated for a second period of time, wherein at least a portion of the first period of time overlaps with the second period of time.
  • heating takes places more than once for the first composition, or for the second composition, or for both.
  • the first composition and the second composition are heated at different temperatures.
  • the first composition and the second composition are heated using different means.
  • the first composition and the second composition are heated for different periods of time.
  • heating the first composition causes at least partial heating of the second composition, for example, via conduction.
  • heating causes densification of the first composition, or the second composition, or both.
  • the first composition is heated to achieve partial densification resulting in a modified first SRT; and then the first and second compositions are heated such that the difference between the modified first SRT and the second SRT is no greater than 75% of the first modified SRT.
  • the first composition is heated to achieve partial densification resulting in a modified first SRT
  • the second composition is heated to achieve partial densification resulting in a modified second SRT; and then the first and second compositions are heated such that the difference between the modified first SRT and the second modified SRT is no greater than 75% of the first modified SRT.
  • the fuel cell comprises a third composition having a third SRT.
  • the third composition is heated such that the difference between the first SRT and the third SRT is no greater than 75% of the first SRT.
  • the third composition is heated to achieve partial densification resulting in a modified third SRT; and then the first and second and third compositions are heated such that the difference between the first SRT and the modified third SRT is no greater than 75% of the first SRT.
  • the first and second and third compositions are heated to achieve partial densification resulting in a modified first SRT, a modified second SRT, and a modified third SRT; and then the first and second and third compositions are heated such that the difference between the modified first SRT and the modified second SRT is no greater than 75% of the modified first SRT and the difference between the modified first SRT and the modified third SRT is no greater than 75% of the modified first SRT.
  • the method produces a crack free electrolyte in the fuel cell.
  • heating is performed in situ. In various embodiments, heating causes sintering or co-sintering or both. In various embodiments, heating takes place for no greater than SO minutes, or no greater than 30 seconds, or no greater than 30 milliseconds.
  • a process flow diagram is shown for forming and heating at least a portion of a fuel cell.
  • 810 represents forming composition 1.
  • 820 represents heating composition 1 at temperature T1 for time tl.
  • 830 represents forming composition 2.
  • 840 represents heating composition 1 and composition 2 simultaneously at temperature T2 for time t2, wherein at T2, the difference between SRT of composition 1 and SRT of composition 2 is no greater than 75% of SRT of composition 1.
  • 840 represents heating composition 1 and composition 2 simultaneously at temperature T2 and T2' (for example, using different heating mechanisms) for time t2, wherein at T2 and T2', the difference between SRT of composition 1 and SRT of composition 2 is no greater than 75% of SRT of composition 1.
  • Example 1 Making a fuel cell stack.
  • Example 1 is illustrative of the preferred method of making a fuel cell stack.
  • the method uses an AMM model no. 0012323 from Ceradrop and an EMR model no. 092309423 from Xenon Corp.
  • An interconnect substrate is put down to start the print.
  • an anode layer is made by the AMM.
  • This layer is deposited by the AMM as a slurry A, having the composition as shown in the table below.
  • This layer is allowed to dry by applying heat via an infrared lamp.
  • This anode layer is sintered by hitting it with an electromagnetic pulse from a xenon flash tube for 1 second.
  • An electrolyte layer is formed on top of the anode layer by the AMM depositing a slurry B, having the composition shown in the table below. This layer is allowed to dry by applying heat via an infrared lamp. This electrolyte layer is sintered by hitting it with an electromagnetic pulse from a xenon flash tube for 60 seconds.
  • a cathode layer is formed on top of the electrolyte layer by the AMM depositing a slurry C, having the composition shown in the table below. This layer is allowed to dry by applying heat via an infrared lamp. This cathode layer is sintered by hitting it with an electromagnetic pulse from a xenon flash tube for 1/2 second.
  • An interconnect layer is formed on top of the cathode layer by the AMM depositing a slurry D, having the composition shown in the table below. This layer is allowed to dry by applying heat via an infrared lamp. This interconnect layer is sintered by hitting it with an electromagnetic pulse from a xenon flash tube for 30 seconds. [247] These steps are then repeated 60 times, with the anode layers being formed on top of the interconnects. The result is a fuel cell stack with 61 fuel cells.
  • Example 4 CGO in water.
  • an electrolyte 1201 (YSZ) is printed and sintered on an electrode 1202 (NiO-YSZ).
  • the scanning electron microscopy image shows the side view of the sintered structures, which demonstrates gas-tight contact between the electrolyte and the electrode, full densification of the electrolyte, and sintered and porous electrode microstructures.
  • Example 8 Fuel cell stack configurations.
  • a 48-Volt fuel cell stack has 69 cells with about 1000 Watts of power output.
  • the fuel cell in this stack has a dimension of about 4 cm x 4 cm in length and width and about 7 cm in height.
  • a 48-Volt fuel cell stack has 69 cells with about 5000 Watts of power output.
  • the fuel cell in this stack has a dimension of about 8.5 cm x 8.5 cm in length and width and about 7 cm in height.

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  • Chemical & Material Sciences (AREA)
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  • Manufacturing & Machinery (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Ceramic Engineering (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Inorganic Chemistry (AREA)
  • Fuel Cell (AREA)
  • Inert Electrodes (AREA)

Abstract

La présente invention concerne un procédé destiné à fabriquer un objet consistant à mélanger des particules à un liquide pour former une dispersion ; à déposer la dispersion sur un substrat pour former une couche ; et à traiter la couche pour entraîner le frittage d'au moins une partie des particules, les particules ayant une répartition de taille qui a au moins une des caractéristiques suivantes : (a) ladite répartition de taille comprend D10 et D90, 10 % des particules ayant un diamètre qui n'est pas supérieur à D10 et 90 % des particules ayant un diamètre qui n'est pas supérieur à D90, D90/D10 étant compris entre 1,5 et 100 ; ou (b) ladite répartition de taille étant bimodale de sorte que la taille moyenne de particules dans le premier mode est d'au moins 5 fois la taille moyenne de particules dans le deuxième mode ; ou (c) ladite répartition de taille comprend D50, 50 % des particules ayant un diamètre qui n'est pas supérieur à D50, D50 n'étant pas supérieur à 100 nm.
EP19886007.4A 2018-11-12 2019-11-12 Procédé de fabrication à contrôle de taille de particules Pending EP3881384A4 (fr)

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US201862758778P 2018-11-12 2018-11-12
US201862767413P 2018-11-14 2018-11-14
US201862768864P 2018-11-17 2018-11-17
US201862771045P 2018-11-24 2018-11-24
US201862773071P 2018-11-29 2018-11-29
US201862773912P 2018-11-30 2018-11-30
US201862777338P 2018-12-10 2018-12-10
US201862777273P 2018-12-10 2018-12-10
US201862779005P 2018-12-13 2018-12-13
US201862780211P 2018-12-15 2018-12-15
US201862783192P 2018-12-20 2018-12-20
US201862784472P 2018-12-23 2018-12-23
US201862786341P 2018-12-29 2018-12-29
US201962791629P 2019-01-11 2019-01-11
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US201962798344P 2019-01-29 2019-01-29
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US201962808644P 2019-02-21 2019-02-21
US201962809602P 2019-02-23 2019-02-23
US201962814695P 2019-03-06 2019-03-06
US201962819374P 2019-03-15 2019-03-15
US201962819289P 2019-03-15 2019-03-15
US201962824229P 2019-03-26 2019-03-26
US201962825576P 2019-03-28 2019-03-28
US201962827800P 2019-04-01 2019-04-01
US201962834531P 2019-04-16 2019-04-16
US201962837089P 2019-04-22 2019-04-22
US201962839587P 2019-04-26 2019-04-26
US201962840381P 2019-04-29 2019-04-29
US201962844126P 2019-05-07 2019-05-07
US201962844127P 2019-05-07 2019-05-07
US201962847472P 2019-05-14 2019-05-14
US201962849269P 2019-05-17 2019-05-17
US201962852045P 2019-05-23 2019-05-23
US201962856736P 2019-06-03 2019-06-03
US201962863390P 2019-06-19 2019-06-19
US201962864492P 2019-06-20 2019-06-20
US201962866758P 2019-06-26 2019-06-26
US201962869322P 2019-07-01 2019-07-01
US201962875437P 2019-07-17 2019-07-17
US201962877699P 2019-07-23 2019-07-23
US201962888319P 2019-08-16 2019-08-16
US201962895416P 2019-09-03 2019-09-03
US201962896466P 2019-09-05 2019-09-05
US201962899087P 2019-09-11 2019-09-11
US201962904683P 2019-09-24 2019-09-24
US201962912626P 2019-10-08 2019-10-08
US201962925210P 2019-10-23 2019-10-23
US201962927627P 2019-10-29 2019-10-29
US201962928326P 2019-10-30 2019-10-30
US16/674,580 US20200176803A1 (en) 2018-11-06 2019-11-05 Method of Making Fuel Cells and a Fuel Cell Stack
US16/674,695 US11735755B2 (en) 2018-11-06 2019-11-05 System and method for integrated deposition and heating
US16/674,657 US11575142B2 (en) 2018-11-06 2019-11-05 Method and system for making a fuel cell
US16/674,629 US11557784B2 (en) 2018-11-06 2019-11-05 Method of making a fuel cell and treating a component thereof
PCT/US2019/060838 WO2020102140A1 (fr) 2018-11-12 2019-11-12 Procédé de fabrication à contrôle de taille de particules

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