Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
  • H01M8/04067—Heat exchange or temperature measuring elements, thermal insulation, e.g. heat pipes, heat pumps, fins
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
  • H01M50/20—Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders
  • H01M50/233—Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders characterised by physical properties of casings or racks, e.g. dimensions
  • H01M50/24—Mountings; Secondary casings or frames; Racks, modules or packs; Suspension devices; Shock absorbers; Transport or carrying devices; Holders characterised by physical properties of casings or racks, e.g. dimensions adapted for protecting batteries from their environment, e.g. from corrosion
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
  • H01M8/2465—Details of groupings of fuel cells
  • H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
  • H01M8/2465—Details of groupings of fuel cells
  • H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
  • H01M8/2475—Enclosures, casings or containers of fuel cell stacks
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
  • H01M2008/1293—Fuel cells with solid oxide electrolytes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M2300/00—Electrolytes
  • H01M2300/0017—Non-aqueous electrolytes
  • H01M2300/0065—Solid electrolytes
  • H01M2300/0068—Solid electrolytes inorganic
  • H01M2300/0071—Oxides
  • H01M2300/0074—Ion conductive at high temperature
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
  • H01M8/04014—Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
  • H01M8/04014—Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
  • H01M8/04022—Heating by combustion
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
  • H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
  • H01M8/249—Grouping of fuel cells, e.g. stacking of fuel cells comprising two or more groupings of fuel cells, e.g. modular assemblies
• • 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
  • Y02E60/10—Energy storage using batteries
• • 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

• the invention relates to heat controlled, solid oxide electrolyte, fuel cell generators, and to an array of such generators disposed in a mono-container shell, for use with a variety of auxiliary components in a power genera- tion system of the lOOkW to 50MW plus capacity.
• Fuel cell based, electrical generator apparatus utilizing solid oxide electrolyte fuel cells (“SOFC”) disposed within a housing and surrounded by insulation are well known, and taught, for example, by U.S. Patent Nos: 4,395,468 (Isenberg) and "Solid Oxide Fuel Cell", Westinghouse Electric Corporation, October 1992, for tubular SOFC; 4,476,196 (Poppel, et al.) for flat plate SOFC; and 4,476,198 (Ackerman, et al.) for "corrugated” SOFC, all herein incorporated by reference .
• SOFC solid oxide electrolyte fuel cells
• the tubular type fuel cells can comprise an open or closed ended, axially elongated, ceramic tube air electrode material, which can be deposited on a ceramic support tube, completely covered by thin film ceramic, solid electrolyte material.
• the electrolyte is substantially covered by cermet fuel electrode material, except for a thin, axially elongated, interconnection material.
• the flat plate type fuel cells can comprise a flat array of electrolyte and interconnect walls, where electrolyte walls contain thin, flat layers of cathode and anode materials sandwiching an electrolyte.
• the "corrugated" plate type fuel cells can comprise a triangular or corrugated honeycomb array of active anode, cathode, electrolyte and interconnect materials.
• Other fuel cells not having a solid electrolyte, such molten carbonate fuel cells are also well known, and can be insulated using the mono-container of this inven- tion.
• pre-heated, compressed air is supplied to a SOFC along with fuel, to produce electric power and a hot gas, which gas is further heated by combustion of unreacted fuel and oxygen remaining in the hot gas.
• This higher temperature gas is directed to a topping combustor that is supplied with a second stream of fuel, to produce a still further heated gas that is then expanded in a turbine .
• U.S. Patent No. 4,622,275 (Noguchi et al . ) also describes a fuel cell power plant, where reformed, reactive fuel is fed to an anode of the cell, an expansion turbine connected to a compressor feeds compressed gas into the cathode of the cell, which compressed gas is mixed with anode exhaust gas which had been combusted.
• the invention resides in a self- cooling, mono-container fuel cell generator apparatus, characterized by having a layer of interior insulation, a layer of exterior insulation, and a single housing having sides placed between the insulation layers, where a plurality of fuel cells containing electrodes and electrolyte are surrounded by the interior insulation, said generator capable of operating at interior temperatures over about 650°C, and said combination of interior and exterior insulation layers having the ability to control the temperature of the housing below the degradation temperature of the housing material.
• the housing material could be cast, specialized concrete with appropriate filler materials, molded ceramic, a variety of low-cost commercial steels, or the like.
• the housing will be a single, discrete (including composite or laminated) layer, for example, molded ceramic or concrete, with an optional, thin, contacting stainless or carbon steel exterior sheeting componen .
• Using a combination of interior and exterior insulation, to control fuel cell generator housing temperature allows cost and performance advantages, even though the interior insulation may be unprotected, by an interior housing, cannister or the like, against contacting gaseous fuel and fuel combustion products and lose substantial insulating properties.
• the fuel cells will generally operate at temperatures over about 650°C, usually over about 650°C and up to about 1250°C.
• the housing configuration can be square, circular or other geometry, and the fuel cells can operate in the "pressurized" mode, that is over about 2 atmospheres, or about 28.5 pounds per sq.
• the invention also broadly resides in a self- cooling, mono-container fuel cell generator apparatus characterized by having: a layer of interior insulation; a layer of exterior insulation; and a single metal housing having top, bottom and side sections with at least the side section of the housing disposed between the insulation layers, said side section having cooling ducts therein, which ducts in the side section communicate to a source of cooling liquid or gas; a plurality of fuel cells containing electrodes and electrolyte surrounded by the interior insulation; a gaseous oxidant inlet; and a gaseous fuel inlet connected to fuel channels to allow fuel passage to the fuel cells.
• gaseous oxidant channels from the oxidant inlet can connect to the cooling ducts to allow gaseous oxidant passage through the cooling ducts to the fuel cells, the gaseous oxidant acting as a cooling gas.
• the interior insulation is subject to contact by interior gases;
• a bottom air plenum connects the oxidant inlet manifold to the cooling ducts, which ducts communicate with a top air plenum which can pass gaseous oxidant to the fuel cells; and an ejector can pass fuel from the fuel inlet to the fuel cells.
• tubular, flat plate and other type high temper- ature fuel cells can be utilized within the mono-container, and a variety of solid, liquid, matrix electrolytes can be used with the fuel cells.
• These generators eliminate use of dual housings; substantially reducing cost and space requirements .
• the generator can operate at interior temperatures up to about 1250°C in a flow of fuel, and oxidant such as oxygen or air, and will also have associated with it and working in cooperation with at least three well known auxiliaries, such as controls; an oxygen or air pre-heater; a fuel gas compressor; a fuel desulfurizer; an oxygen or air compressor which may be operably connected to a turbine; a source of fuel gas; heat exchangers; and a heat recovery unit to recover heat from the hot fuel cell exhaust gases; and a topping combustor, to provide an electrical power generation system.
• auxiliaries such as controls
• an oxygen or air pre-heater such as a fuel gas compressor
• a fuel desulfurizer an oxygen or air compressor which may be operably connected to a turbine
• a source of fuel gas heat exchangers
• a heat recovery unit to recover heat from the hot fuel cell exhaust gases
• topping combustor to provide an electrical power generation system.
• the invention also resides in a power generation system characterized by containing a plurality of self- cooling, mono-container fuel cell generator apparatus, each generator having: a layer of interior insulation; a layer of exterior insulation; a single metal housing between the insulation layers, the housing containing top, bottom and side sections, the side section of the housing having cooling ducts therein; a plurality of fuel cells surrounded by the interior insulation; a fuel inlet and fuel transfer channels connecting to the fuel cells; and an oxidant inlet and oxidant transfer channels connecting to the fuel cells; where the plurality of generators are positioned next to each other to provide a close packed array of generators, each generator capable of operating at interior temperatures over about 700°C, said array having exterior generator housing side sections and interior generator housing side sections, and where the interior side sections can be cooled by gas or liquid passing through the cooling ducts at the boundary of the interior side sections of the array.
• This type power system could be, for example, part of an integrated, coal gasification/fuel cell-steam turbine combination power plant, featuring a plurality of coal gasifiers and fuel cell generator arrays or power blocks with associated DC/AC conversion switchgear.
• This system solves overheating problems associated with an array of close packed generators, and results in substantial internal cost and space savings .
• FIG. 1 which best shows the invention, is a three dimensional, cut away view of one embodiment of a single fuel cell generator, having a -nono-container whose cooling is controlled by a combination of interior and exterior insulation
• FIG. 2 is a three imensional, cut away view of another embodiment of a single fuel cell generator, having a mono-container with internal, integral cooling ducts, whose cooling is controlled by the combination of cooling ducts and interior and exterior insulation;
• FIG. 3 shows a three dimensional, cut away view of one embodiment of the mono-container of FIG. 2, at a slightly different angle for illustrative purposes, more clearly showing the internal cooling ducts and internal insulation of the generator;
• FIG. 4 shows a cross sectional view through line
• FIG. 5 shows a cross-sectional view of the fuel cell generator of FIG. 2, showing oxidant and fuel flow paths;
• FIG. 6 shows a partial cross-sectional view of one embodiment of an array of ten close packed mono-container generators which provides a compact power block of up to 1.5 MW capacity, with cooling by means of interior and exterior insulation, and oxidant cooling ducts in the interior of the array as well as around the periphery of the array;
• FIG. 7 shows one embodiment of a 300 MW integrated coal gasification/fuel cell-steam turbine power plant, utilizing a plurality of power blocks, such as shown in FIG. 6.
• FIG. 1 of the drawings one type of fuel cell generator 10 is shown.
• the tubular design would make it particularly useful for fuel cell operation at over atmospheric pressures.
• the interior 12 of the generator 10 would contain a plurality of fuel cells (not shown) which could be of various configurations, for example, flat, corrugated, or tubular, utilizing a variety of electrolytes operable at relatively high temperatures, for example, a phosphoric acid matrix or a solid oxide ceramic, disposed between electrodes, such as air electrodes (the electrode contacted by oxidant such as air) and fuel electrodes (the electrode contacted by fuel, such as reformed coal gas or reformed natural gas) .
• a phosphoric acid matrix or a solid oxide ceramic disposed between electrodes, such as air electrodes (the electrode contacted by oxidant such as air) and fuel electrodes (the electrode contacted by fuel, such as reformed coal gas or reformed natural gas) .
• the fuel cells would have associated interconnections and power leads, feed oxidant transfer tubing, feed fuel transfer tubing, and the like. These fuel cells are surrounded by interior insulation layer 14. Exterior insulation layer 16 surrounds at least the sides 18 of the generator housing 20 (here shown as concrete) and will usually also cover the top 22 of the generator housing.
• the embodiment of the housing shown in FIG. 1 is a "composite", including the main housing 20 of, for example, specialized concrete, such as carbon fiber reinforced concrete or ceramic fiber reinforced concrete for higher temperatures applications, with an optional, contacting, thin sheet of metal such as steel 20', with possible rib or top side reinforcements (not shown) .
• the housing even if one or more thin component sheets 20' are used, is still defined herein as a single housing or mono-container.
• the interior insulation may be in contact with hot fuel gas, mixtures of reacted oxidant and fuel, and possi- bly hot oxidant gas, at various places within the generator, at temperatures up to 1250°C and possibly at pressures from 28.5 psi up to 220 psi. (2.0 kg/sq cm up to 15.5 kg/sq cm) .
• the insulation must be selected from a limited set of materials that can withstand these tempera - tures and still provide adequate thermal protection for the housing.
• the insulation generally should be substantially silica-free to avoid possible silica contamination of the fuel cells, especially SOFC, that could potentially degrade performance. Therefore, the interior insulation 14 should be, preferably, of a type of high purity alumina fibers. This alumina material provides good insulation properties, and is available in high purity where silica is minimized. This alumina insulation is quite porous, and does lose some insulating properties when it becomes exposed to reformed fuel found in the typical fuel cell stack.
• the exterior insulation 16 can be silica, fiberglass, alumina, or the like, and it will generally be exposed to ambient air.
• the thickness ratio of (interior insulation) : (exterior insula- tion) should generally be from about (1) : (.2) to (1) : (3) .
• a ratio of (1):(.35) is utilized.
• the housing 20 which can be concrete, concrete-metal composite, metal such as steel, or ceramic, at the lowest safe operating temperature to minimize the quantity of the expensive interior insulation.
• the interior insulation is generally more expensive due to the preferred high purity requirements.
• the total thickness required for 14 and 20 is determined by overall heat loss permitted, and the desired thermal efficiency of the fuel cell stack.
• Active cooling of the structural barrier 20 provides an additional feature of the design.
• the cooling can easily control the temperature of 20 because of the relatively large thermal resistance of interior insulation 14.
• the coolant could be incoming air used to supply the fuel cell stack, a separate cooling source such as water, chemicals or gases which have to be heated anyway for use or treatment, and thus, just about any liquid or gas economically available.
• the fuel cells used inside the generator shown in FIG. 1 or FIG. 2 can be solid oxide electrolyte or molten carbonate fuel cells of any type or configuration.
• tubular, solid oxide electrolyte fuel cells will be discussed as an exemplary type useful in this invention, and the description hereinafter will generally relate to that type, which shall in no way be considered limiting as to the scope of the invention.
• Solid oxide fuel cells are highly efficient devices that convert chemical energy into electricity. They operate at atmospheric or elevated pressures at a temperature of approximately 1000°C to produce electricity using a variety of fossil fuels such as coal derived fuel gas, natural gas, or distillate fuel.
• the temperature of the exhaust gases from the cells is between 500°C to 850°C, a temperature which is attractive for cogeneration applications or for use in bottoming cycles for all-electric central station power plants.
• An operating SOFC readily conducts oxygen ions from an air electrode (cathode) , where they are formed, through a solid electrolyte to a fuel electrode (anode) . There they react with carbon monoxide (CO) and hydrogen (H 2 ) contained in the fuel gas to deliver electrons and produce electricity.
• the tubular SOFC features a porous air electrode made of doped lanthanum manganite.
• a gas-tight electrolyte of yttria-stabilized zirconia covers the air electrode, except in a strip about 9mm wide along the entire active cell length. This strip of exposed air electrode is covered by a thin, dense, gas tight layer of doped lanthanum chromite. This layer, termed the cell interconnection, serves as the electric contacting area to an adjacent cell or to a power contact.
• the fuel electrode is a nickel-zirconia cermet and covers the electrolyte surface except in the vicinity of the interconnection.
• air is introduced into the fuel cell, generally through an air injector tube.
• the air discharged near the closed end of the cell, flows through the annular space formed by the cell and its coaxial injector tube.
• Fuel flows on the outside of the cell.
• the gas-imper- vious electrolyte does not allow nitrogen to pass from the air side to the fuel side, hence the fuel is oxidized in a nitrogen free environment, averting the formation of NOx.
• the remaining fuel is reacted with the air stream exiting the cell, thereby providing additional useful heat. Reformation of natural gas and other fuels containing hydrocarbons can be accomplished, if desired, within the generator. Incoming fuel can be reformed to H 2 and CO within the generator, eliminating the need for an external reformer. All the gas flows and reactions are controlled within the generator apparatus.
• individual cells are "bundled" into an array of series-parallel electrically connected fuel cells, forming a semi-rigid structure that is a basic generator building block.
• the individual bundles are arrayed in series or parallel to build generator voltage or current, depending on the application, and to form submodules.
• the parallel electri- cal connection of the cells within a bundle enhances generator reliability.
• Submodules are further combined in either parallel or series connections to form the generator module.
• Exterior insulation layer 16 surrounds at least the sides of the generator housing 20, which can be made solely of iron, steel, stainless steel, nickel alloy or other suitable metal.
• the generator is devoid of an interior cylinder, cannister, or wall adjacent to and interior of the interior insulation 14.
• the exterior insulation 16 usually also covers the top 22 of the generator housing as shown.
• an oxidant distribution manifold 24 where, for example, air can be fed into the bottom of the generator.
• Combusted exhaust gas manifold 26 can exit spent fuel and spent oxidant.
• a fuel such as previously described, can be fed to the top of the generator through a fuel inlet means, such as piping 28.
• FIG. 3 A cut away section of the top 22, shows top housing 20 with integral cooling ducts 30 and also, interior insulation 14.
• FIG. 3 A detailed drawing of the bottom part of the housing 20 is shown in FIG. 3.
• This housing 20 is a self- cooling, mono-container type, holding interior insulation 14.
• the housing 20 has at least its sides disposed between interior and exterior insulation, as shown in FIG. 2 and in FIG 4.
• Cooling ducts 30 are shown in the sides of the housing 20, preferably surrounding the housing as shown.
• the bottom of these cooling ducts 30 communicate to a gaseous oxidant inlet, such as the lower air plenum 32, from the oxidant distribution manifold 24.
• oxidant may be fed directly to the fuel cells similarly to the fuel, and cooling can be accomplished by continuous flow of water or other liquids or gases.
• the interior insulation in all cases is subject to contact by interior gases.
• FIG. 3 is shown as a rounded off square, but it can be other configurations, for example the side sections could be a continuous tube.
• FIG. 4 is a cross section of the insulated generator of FIG. 2 along line 4-4, showing fuel cell bundles 34, each bundle contains a plurality of interconnected fuel cells 36, here shown as of the tubular SOFC type, with electrodes and sandwiched electrolyte.
• Fuel would enter fuel inlet piping 28 and pass, preferably to one or more ejectors 38, which are better shown in FIG. 5, where recirculation gases may inject-mix with feed fuel, to provide a stream useful in the reforming section 40 and to otherwise provide optimal operating conditions.
• the fuel stream 42 then exits reformer 40 and passes through a fuel plenum 44 and into fuel supply lines which transfer or pass at least partly reformed fuel to the outside of fuel cells 36, as shown in FIG. 5, where the fuel reacts along the elongated fuel electrode surface on the exterior of the tubular fuel cells 36.
• oxidant enters air plenum 32 as oxidant stream 48 passing upward through cooling ducts 30 to a top air distribution plenum 50.
• the oxidant stream then is transferred and passes downward via individual oxidant feed tubes 52 into the bottom interior of each fuel cell 36, where, as is well known in the art, the oxidant reverses flow and passes in the annular space between the oxidant feed tube and the interior air electrode, where it reacts along the air electrode interior surface.
• the reacted oxidant finally enters a combustion section 54 (flow not shown) as spent oxidant.
• the spent oxidant then combusts with spent fuel to provide exhaust gas 56, part of which may be recirculated to the ejector 38.
• the rest of the exhaust 56 gas passes through exhaust ducts 58 into the exhaust gas manifold 26, shown in FIG. 2. Further details on these flow patterns as well as use of an ejector system can be found in U.S. Patent No. 5,169,730 (Reichner) .
• an array 60 of ten, insulated, mono-containers are shown as providing a power block.
• the housings 20, containing cooling ducts 30, are surrounded by exterior insulation 16 (fuel cell generator internals are not shown for the sake of clarity) .
• Exterior generator side sections 62, as well as interior side sections 64 can be cooled by gaseous oxidant passage through the cooling ducts 30. This cooling is especially important at the center interior portions 66 of the array 60, solving overheating problems associated with a close packed generator array and allowing use of a wider section of steels for the container housings 20. Without cooling between the modules, the space between modules would reach stack temperatures of 1000 °C or over. Stable metallic structures for long term use at these temperatures might require exotic, very expensive alloys.
• the exhaust gas manifolds 26, shown more clearly in FIG. 2 are shown connected together from generator to generator. Fuel feed piping 28 is also shown connected.
• FIG. 7 depicts a 300 MW, integrated coal gasification/fuel cell steam turbine power plant 70.
• Coal gasification unit 72, air separation (oxygen) plant 74, DC/AC conversion and electrical switch gear and power conditioning unit 76 are shown, along with five, 50, 000-ton coal storage silos 78.
• the fuel feed from the coal gasification units can operate eight SOFC power block arrays 60, described previously, each containing 12 SOFC generators or modules, which in turn are associated with a heat recovery steam turbine 80 and heat recovery steam generator 82.
• the SOFC blocks can be integrated into a system utilizing a turbine.
• a compressor could compress preheated air which could be supplied to the fuel cells.
• the hot gas from the power blocks could be pumped at high pressure to a combustor, producing further heated hot gas that could be expanded in a turbine to produce power.
• the turbine could in turn run a compressor for pressurizing the oxidant stream, as in U.S. Patent No. 3,972,731 (Bloomfield et al . ) .
• the hot gas from the power blocks could be directed to a turbine by way of a topping combustor that is supplied with fuel, to produce a still further heated hot gas that is then passed to and expanded in a turbine apparatus as in U.S. Patent No. 5,413,879 (Domeracki et al . ) .
• the major components of the system would be a compressor, a turbine, a rotor by which the turbine drives the compressor as well as an electrical generator, a fuel pre-heater, an air pre-heater, a fuel desulfurizer, a solid oxide fuel cell generator with a combustion chamber, a topping combustor and an exhaust stack.
• the compressor which includes rows of stationary vanes and rotating blades, inducts ambient air and produces compressed air.
• the compressed air after flowing through a topping combustor, is heated by the air pre-heater.
• the air pre-heater which may be of the finned tube type, has heat transfer surfaces that allow heat to be transferred from the turbine exhaust gas discharged by the fuel pre-heater, to the compressed air, thereby producing heated compressed air.
• the compressed air can be heated into approximately the 500°C-600°C.
• the heated compressed air is then directed to the solid oxide fuel cell generator.
• Gaseous fuel which may be natural gas or a coal derived fuel gas, is driven by a pump through the fuel pre- heater.
• the fuel pre-heater which may be of the finned tube type, has heat transfer surfaces that allow heat to be transferred from the exhaust gas discharged by the turbine to the fuel, thereby producing heated fuel.
• the fuel can be heated to approximately 400°C.
• the heated fuel is then directed to a desulfurizer, which may comprise a vessel containing a bed cf sulfur sorbent through which the fuel flows.
• the fuel exiting from the desulfurizer preferably, has less than 0.1 ppm of sulfur. While FIG. 6 and FIG. 7 have been generally described using SOFC, other types of fuel cell could be used in such systems, as described previously. This is only one design that could use the close packed power block arrays of this invention.
• Cooling with process air eliminates the requirement for separate liquid or liquid/air cooling loops and the solid electrolyte eliminates the problems associ- ated with the management of liquid electrolytes.

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• 1996
  • 1996-12-26 CA CA002247466A patent/CA2247466A1/en not_active Abandoned
  • 1996-12-26 AU AU16890/97A patent/AU1689097A/en not_active Abandoned
  • 1996-12-26 HU HU9902162A patent/HUP9902162A2/hu unknown
  • 1996-12-26 CN CN96180120A patent/CN1209220A/zh active Pending
  • 1996-12-26 WO PCT/US1996/020749 patent/WO1998029917A1/en not_active Application Discontinuation
  • 1996-12-26 EP EP96945667A patent/EP0894344A1/de not_active Withdrawn

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