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US20050132650A1 - Fast light-off catalytic reformer - Google Patents

Fast light-off catalytic reformer Download PDF

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Publication number
US20050132650A1
US20050132650A1 US11046298 US4629805A US2005132650A1 US 20050132650 A1 US20050132650 A1 US 20050132650A1 US 11046298 US11046298 US 11046298 US 4629805 A US4629805 A US 4629805A US 2005132650 A1 US2005132650 A1 US 2005132650A1
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Prior art keywords
fuel
catalyst
reformate
air
reformer
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Abandoned
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US11046298
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Galen Fisher
John Kirwan
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Delphi Technologies Inc
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Delphi Technologies Inc
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0207Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
    • B01J8/0221Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a cylindrical shaped bed
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00548Flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00716Means for reactor start-up
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00191Control algorithm
    • B01J2219/00193Sensing a parameter
    • B01J2219/00195Sensing a parameter of the reaction system
    • B01J2219/002Sensing a parameter of the reaction system inside the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00191Control algorithm
    • B01J2219/00211Control algorithm comparing a sensed parameter with a pre-set value
    • B01J2219/00213Fixed parameter value
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00191Control algorithm
    • B01J2219/00222Control algorithm taking actions
    • B01J2219/00227Control algorithm taking actions modifying the operating conditions
    • B01J2219/00229Control algorithm taking actions modifying the operating conditions of the reaction system
    • B01J2219/00231Control algorithm taking actions modifying the operating conditions of the reaction system at the reactor inlet
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of products other than chlorine, adipic acid, caprolactam, or chlorodifluoromethane, e.g. bulk or fine chemicals or pharmaceuticals
    • Y02P20/52Improvements relating to the production of products other than chlorine, adipic acid, caprolactam, or chlorodifluoromethane, e.g. bulk or fine chemicals or pharmaceuticals using catalysts, e.g. selective catalysts

Abstract

A fast light-off catalytic reformer and method includes at least one preferably substantially cylindrical reactor tube having an inlet for receiving a flow of fuel and a flow of air, a reforming catalyst disposed within the reactor tube for converting the fuel and air to a reformate stream, and an outlet for discharging the produced reformate stream. An ignition device disposed within the reactor tube initiates an exothermic reaction between the fuel and air. Heat generated thereby provides fast light-off of the reforming catalyst. An associated control system selects fuel and air flow delivery rates and operates the ignition device to achieve fast light-off of the reforming catalyst at start-up and to maintain the catalyst at a temperature sufficient to optimize reformate yield. The rapid production of high yields of reformate is particularly suitable for use in an on-board reforming strategy for meeting SULEV emissions with spark-ignition engines, especially with larger, higher emitting vehicles.

Description

    TECHNICAL FIELD
  • [0001]
    The present invention relates to a catalytic reformer and method for converting a hydrocarbon stream to a reformate fuel stream comprising hydrogen, and more particularly relates to a fast light-off catalytic reformer and method for rapid production of reformate fuel. The present invention is particularly suitable for on-board production of reformate for hydrogen cold-start in an internal combustion engine. The present invention is also suitable for providing reformate to a fuel cell such as a solid oxide fuel cell.
  • BACKGROUND OF THE INVENTION
  • [0002]
    A catalytic hydrocarbon fuel reformer converts a fuel stream comprising, for example, natural gas, light distillates, methanol, propane, naphtha, kerosene, gasoline, diesel fuel, or combinations thereof, and air, into a hydrogen-rich reformate fuel stream comprising a gaseous blend of hydrogen, carbon monoxide and nitrogen (ignoring trace components). In the reforming process, the raw hydrocarbon fuel stream is typically percolated through a catalyst bed or beds contained within reactor tubes mounted in the reformer vessel. The catalytic conversion process is typically carried out at elevated catalyst temperatures in the range of about 1200° F. to about 1600° F.
  • [0003]
    In most reformers of this type, hot burner gas generated at a burner generally disposed within the reformer vessel accumulates in a primary (typically, upper) plenum within the vessel, contacting and heating the outer surface of the reactor tubes, thereby heating the catalyst. The hot burner gas may be directed through a cylindrical sleeve surrounding the lower portion of each reactor tube, so that the hot burner gas travels in close contact with outer surfaces of the reactor tubes and effective heat transfer occurs. Hot burner gas from the primary plenum flows through a narrow annular passage between the internal wall of the sleeve and the external wall of each reactor tube, and into a secondary (lower) plenum, from which it is discharged. Seal plates or insulation may be employed to prevent bypass of the hot burner gases around the sleeve.
  • [0004]
    The produced hydrogen-rich reformate stream may be used, for example, as the fuel gas stream feeding the anode of an electrochemical fuel cell after passing the reformate stream through a water gas shift reactor and other purification means such as a carbon monoxide selective oxidizer. Reformate is particularly well suited to start up a solid oxide fuel cell (SOFC) system because the purification step for removal of carbon monoxide is not required for an SOFC.
  • [0005]
    The hydrogen-rich reformate stream may also be used as a hydrogen fuel to fuel an engine. Hydrogen-fueled vehicles are of interest as low-emissions vehicles because hydrogen as a fuel or a fuel additive can significantly reduce air pollution and can be produced from a variety of fuels. Hydrogen provides the capability to run an engine with very lean fuel-air mixtures that greatly reduce production of NOx. Small amounts of supplemental hydrogen fuel may allow conventional gasoline internal combustion engines to reach nearly zero emissions levels. Commonly assigned, co-pending U.S. patent application Ser. No. ______ (Attorney Docket No. DP-301698) of Kirwan et al., entitled “System And Controls For Near Zero Cold Start Tailpipe Emissions In Internal Combustion Engines,” hereby incorporated by reference herein in its entirety, discloses an on-board fuel reformer-engine system employing substantially 100% reformate fueling at start-up for near-zero cold start hydrocarbon and NOx engine emissions. The system and method provides for controlling the supply of one or a combination of reformate, liquid fuel, and air to the engine and exhaust catalyst to achieve low hydrocarbon and NOx emissions over a full range of engine operating conditions.
  • [0006]
    While hydrogen fuel may be stored on-board to provide an instant source of reformate fuel, on-board storage of reformate significantly increases system size, cost and complexity. For example, on-board storage may require high-pressure vessels, cryogenic containers if the hydrogen is to be stored as a compressed gas or liquid, or large volumes and weights if the hydrogen is to be stored as a hydride. In addition, storage of carbon monoxide may be a safety concern. Further, the refill time for hydrogen is substantially longer than that for gasoline when hydrogen is to be stored on-board.
  • [0007]
    What is needed in the art is a reformate-generating device comprising a rapid start up (or “fast light-off”) system. What is further needed in the art is a rapid start-up catalytic reformer for producing reformate suitable for feeding a power generation system such as a fuel cell or engine.
  • SUMMARY OF THE INVENTION
  • [0008]
    A fast light-off catalytic reformer and method is provided. The reformer includes at least one reactor tube having an inlet for receiving a flow of fuel and a flow of air, a reforming catalyst disposed within the reactor tube for converting the fuel and air to a reformate stream, and an outlet for discharging the produced reformate stream. An ignition device is disposed within the reactor tube for initiating an exothermic reaction between the fuel and air and using the heat generated thereby to provide fast light-off of the reforming catalyst. The ignition device may be located at various positions within the reactor tube, as desired, such as, but not limited to, upstream of the reforming catalyst. An associated control system selects fuel and air flow delivery rates and operates the ignition device so as to achieve fast light-off of the reforming catalyst at start-up and to maintain the catalyst at a temperature sufficient to optimize reformate yield.
  • [0009]
    The method includes supplying a flow of premixed fuel and air to the catalytic reformer and igniting the fuel and air within the reactor tube to rapidly heat the reforming catalyst with the heat of combustion. The method also includes controlling the fuel and air delivery rate and the igniting so as to achieve fast light-off at start-up and to maintain the reforming catalyst at a temperature sufficient to optimize reformate yield.
  • [0010]
    The present fast light-off reformer and method advantageously provides a compact and efficient system. The present invention provides the further advantage of reducing the size of a discrete burner and associated system for flowing and exhausting hot burner gases in order to achieve and maintain an effective catalyst temperature.
  • [0011]
    The present fast light-off reformer and method provides the advantage of rapid production of high yields of reformate and is particularly useful for an on-board reforming strategy for meeting SULEV emissions with spark-ignition engines, especially with larger, higher emitting vehicles. The present fast light-off reformer and method is also well suited for providing rapid production of reformate to other power generation systems, such as fuel cells, and is particularly useful for start up and fueling solid oxide fuel cells.
  • [0012]
    These and other features and advantages of the invention will be more fully understood from the following description of certain specific embodiments of the invention taken together with the accompanying drawings.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • [0013]
    Referring now to the drawing, which is meant to be exemplary, not limiting:
  • [0014]
    FIG. 1 is a perspective view, partially in section, of an embodiment of a fast light-off catalytic reformer in accordance with the present invention.
  • DESCRIPTION OF THE PREFERRED EMBODIMENT
  • [0015]
    Turning to FIG. 1, a fast light-off catalytic reformer in accordance with one possible embodiment of the present invention includes a reactor tube 10 having an inlet 12 in a first end for receiving a flow of fuel and a flow of air, shown as combined fuel-air stream 14. Reactor tube 10 may be any shape, but typically comprises a substantially cylindrical reactor tube. While the present description discusses a single reactor tube 10, reforming catalyst 16, and ignition device 22, the present fast light-off reformer may comprise one or more reactor tubes, as desired.
  • [0016]
    Reforming catalyst 16 is disposed within the reactor tube 10. Reforming catalyst 16 may comprise any reforming catalyst suitable for converting the fuel feedstock and air to reformate, including, but not limited to, for example, rhodium, platinum, their alloys, and combinations thereof. Preferably, a protective coating or firewall (not shown) is disposed about catalyst 16. During operation, air and fuel 14 flows through inlet 12 and is converted in catalyst 16 to a hydrogen rich reformate fuel stream 18 that is discharged through outlet 20.
  • [0017]
    Ignition device 22 is disposed within the reactor tube 10 to initiate an exothermic reaction in fuel and air flow 14. Heat generated by this reaction is used to provide fast light-off (i.e., extremely rapid heating) of the reforming catalyst 16. The ignition device may be located upstream of the catalyst, within the catalyst at the front face thereof, or within the catalyst at the rear face of the catalyst. In a preferred embodiment, the ignition device 22 is disposed within the reactor tube 10 upstream of the reforming catalyst 16, i.e., between inlet 12 and reforming catalyst 16. Ignition device 22 may be any device suitable for initiating exothermic reactions between fuel and air 14, including, but not limited to, a catalytic or non-catalytic substrate, such as a wire or gauze, for receiving electric current from a voltage source, a spark plug, a glow plug, or a combination thereof.
  • [0018]
    An associated control system (30) selects and maintains the appropriate fuel and air delivery rates and operates the ignition device 22 so as to achieve fast light-off of the reforming catalyst 16 at start-up and to maintain catalyst 16 at a temperature sufficient to optimize reformate 18 yield. The control means used herein may comprise any of various control means known in the art for providing air and fuel control and metering functions.
  • [0019]
    Excellent reformate yields from the reactor depend upon both a sufficiently high catalyst temperature and the appropriate air-fuel ratio. The optimum air-fuel mixture for producing reformate is very fuel rich, but leaner mixtures provide higher temperatures for rapidly heating the catalyst. The control system varies air-fuel ratio during start-up of the reformer to rapidly obtain both the temperatures and air-fuel mixtures required for high reformate yields.
  • [0020]
    The present fast light-off catalytic reformer and method produce rapid, high yields of reformate fuel. The produced reformate may be bottled in a vessel (40) or used to fuel any number of systems operating partially or wholly on reformate fuel. Such power generation systems (50) may include, but are not limited to, engines such as spark ignition engines, hybrid vehicles, diesel engines, fuel cells, particularly solid oxide fuel cells, or combinations thereof. The present fast light-off reformer and method may be variously integrated with such systems, as desired. For example, the present fast light-off reformer may be employed as an on-board reformer for a vehicle engine operating wholly or partially on reformate, the engine having a fuel inlet in fluid communication with the reformer outlet 20 for receiving reformate 18 therefrom. The present fast light-off reformer and method is particularly suitable for use as an on-board reformer for generating a fast supply of reformate 18 for initial start-up of a system. The present reformer and method is particularly advantageous for hydrogen cold-start of an internal combustion engine, providing a fast supply of hydrogen-rich reformate which allows the engine exhaust to meet SULEV emissions levels immediately from cold-start.
  • [0021]
    While the invention has been described by reference to certain preferred embodiments, it should be understood that numerous changes could be made within the spirit and scope of the inventive concepts described. Accordingly, it is intended that the invention not be limited to the disclosed embodiments, but that it have the full scope permitted by the language of the following claims.

Claims (10)

  1. 1. A fast light-off catalytic reformer comprising:
    a catalytic reformer characterized by at least one reactor tube, said reactor tube having an inlet in a first end for receiving a flow of fuel and a flow of air, a reforming catalyst disposed within said reactor tube for converting said fuel and said air to a reformate stream, and an outlet in a second end for discharging said reformate stream;
    an ignition device disposed within said reactor tube for initiating an exothermic reaction between said fuel and said air and using heat generated thereby to provide fast light-off of said reforming catalyst; and;
    a control system for selecting fuel and air flow rate and operating said ignition device so as to achieve fast light-off of said reforming catalyst at start-up and to maintain said catalyst at a temperature sufficient to optimize reformate yield.
  2. 2. The reformer of claim 1, wherein said ignition device disposed within said reactor tube is located upstream of said reforming catalyst, within said reforming catalyst at the front face of said reforming catalyst, or within said reforming catalyst at the rear face of said reforming catalyst.
  3. 3. The reformer of claim 1, wherein said ignition device comprises a catalytic substrate or a non-catalytic substrate for receiving electric current from a voltage source, a spark plug, a glow plug, or a combination thereof.
  4. 4. A power generation system employing a fast light-off reformer comprising:
    a catalytic reformer characterized by at least one reactor tube, said reactor tube having an inlet in a first end for receiving a flow of fuel and a flow of air, a reforming catalyst disposed within said reactor tube for converting said fuel and said air to a reformate stream, and an outlet in a second end for discharging said reformate stream;
    an ignition device disposed within said reactor tube for initiating an exothermic reaction between said fuel and said air and using heat energy generated thereby to provide fast light-off of said reforming catalyst;
    a control system for selecting fuel and air flow rate and operating said ignition device so as to achieve fast light-off of said reforming catalyst at start-up and to maintain said catalyst at a temperature sufficient to optimize reformate yield; and
    a power generation system operating at least partially on reformate fueling, said power generation system having a fuel inlet in fluid communication with said reformer outlet.
  5. 5. The fast light-off reformer-power generation system of claim 4, wherein said power generation system is an engine, a spark ignition engine, a hybrid vehicle, a diesel engine, a fuel cell, a solid oxide fuel cell, or a combination thereof.
  6. 6. A fast light-off reforming method comprising:
    supplying a flow of fuel and a flow of air to a catalytic reformer, said catalytic reformer characterized by at least one reactor tube having an inlet for receiving said flow of fuel and air, a reforming catalyst disposed within said reactor tube for converting said flow of fuel and air to a reformate stream, and an outlet for discharging said reformate stream;
    igniting said fuel and air within said reactor tube to rapidly heat said reforming catalyst with heat energy generated thereby; and
    controlling said fuel and air supply and said igniting so as to achieve fast light-off of said reforming catalyst at start-up and to maintain said reforming catalyst at a temperature sufficient to optimize reformate yield.
  7. 7. The method of claim 6, wherein said igniting is with an ignition device selected from the group consisting of a catalytic or non-catalytic substrate for receiving an electric current, a spark plug, a glow plug, or a combination thereof.
  8. 8. The method of claim 7, wherein said substrate is wire or gauze.
  9. 9. The method of claim 6, further comprising:
    fueling a power generation system at least partially with said reformate stream.
  10. 10. The method of claim 9, wherein said power generation system is an engine, a spark ignition engine, a hybrid vehicle, a diesel engine, a fuel cell, a solid oxide fuel cell, or a combination thereof.
US11046298 2000-06-27 2005-01-28 Fast light-off catalytic reformer Abandoned US20050132650A1 (en)

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EP2161078A2 (en) 2008-09-05 2010-03-10 Delphi Technologies, Inc. Hydrocarbon reformer substrate having a graded structure for thermal control
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US7082753B2 (en) * 2001-12-03 2006-08-01 Catalytica Energy Systems, Inc. System and methods for improved emission control of internal combustion engines using pulsed fuel flow
US7037349B2 (en) * 2002-06-24 2006-05-02 Delphi Technologies, Inc. Method and apparatus for fuel/air preparation in a fuel cell
US20040171900A1 (en) * 2003-02-28 2004-09-02 Conocophillips Company Method and device for reactions start-up
US7081144B2 (en) * 2003-04-04 2006-07-25 Texaco Inc. Autothermal reforming in a fuel processor utilizing non-pyrophoric shift catalyst
US8337757B2 (en) * 2008-02-07 2012-12-25 Precision Combustion, Inc. Reactor control method
US20090252661A1 (en) * 2008-04-07 2009-10-08 Subir Roychoudhury Fuel reformer
US8439990B2 (en) * 2009-07-21 2013-05-14 Precision Combustion, Inc. Reactor flow control apparatus
US8784515B2 (en) 2010-10-14 2014-07-22 Precision Combustion, Inc. In-situ coke removal
CN105706283A (en) 2013-11-06 2016-06-22 瓦特燃料电池公司 Integrated gaseous fuel cpox reformer and fuel cell systems, and methods of producing electricity
US9624104B2 (en) 2013-11-06 2017-04-18 Watt Fuel Cell Corp. Liquid fuel CPOX reformers and methods of CPOX reforming
CN105705227A (en) 2013-11-06 2016-06-22 瓦特燃料电池公司 Liquid fuel cpox reformer and fuel cell systems, and methods of producing electricity
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