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US20100101465A1 - Method For Injecting Ballast Into An Oxycombustion Boiler - Google Patents

Method For Injecting Ballast Into An Oxycombustion Boiler Download PDF

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Publication number
US20100101465A1
US20100101465A1 US12/578,621 US57862109A US2010101465A1 US 20100101465 A1 US20100101465 A1 US 20100101465A1 US 57862109 A US57862109 A US 57862109A US 2010101465 A1 US2010101465 A1 US 2010101465A1
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US
United States
Prior art keywords
combustion chamber
shielding gas
boiler
gas streams
injected
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.)
Abandoned
Application number
US12/578,621
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English (en)
Inventor
Jacky Laurent
Xavier Paubel
Jacques Mulon
Patrick Jean-Marie Recourt
Ivan Sanchez-Molinero
Remi Pierre Tsiava
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.)
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Original Assignee
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
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
Application filed by LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude filed Critical LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Assigned to L'AIR LIQUIDE SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE reassignment L'AIR LIQUIDE SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: TSIAVA, REMI, LAURENT, JACKY, MULON, JACQUES, PAUBEL, XAVIER, RECOURT, PATRICK, SANCHEZ-MOLINERO, IVAN
Publication of US20100101465A1 publication Critical patent/US20100101465A1/en
Abandoned legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C9/00—Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
    • F23C9/08—Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber for reducing temperature in combustion chamber, e.g. for protecting walls of combustion chamber
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
    • F23L7/007—Supplying oxygen or oxygen-enriched air
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2202/00—Fluegas recirculation
    • F23C2202/40—Inducing local whirls around flame
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2202/00—Fluegas recirculation
    • F23C2202/50—Control of recirculation rate
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23D—BURNERS
    • F23D2900/00—Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/00006—Liquid fuel burners using pure oxygen or O2-enriched air as oxidant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
    • F23L2900/07002—Injecting inert gas, other than steam or evaporated water, into the combustion chambers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L2900/00—Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
    • F23L2900/07005—Injecting pure oxygen or oxygen enriched air
    • 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
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Definitions

  • the present invention relates to a method for injecting fuel, oxidant and ballast into an oxycombustion boiler.
  • the ballast may consist of recycled flue gases (whether cold or not), with the advantage of having flame radiation absorption properties with respect to the predominant gases CO 2 and H 2 O, or other gases or gas mixtures.
  • the shielding gas is meant to be essentially devoid of nitrogen, as this invention is directed toward oxy-combustion in boilers.
  • the goal of this oxy-combustion in boilers is to produce an exhaust stream enriched in CO 2 , and thereby facilitating CO 2 capture.
  • shielding gas envisaged in the present invention are therefore flue gas recycle from oxy-combustion (composed mainly of CO 2 and H 2 O), dried flue gas recycle from oxy-combustion (composed mainly of CO 2 , after condensation of moisture) or steam.
  • a shielding gas stream may also be composed of flue gas recycle, but in such a case this stream would contain a non-negligible content of nitrogen (over 50% in volume).
  • a shielding gas stream may even be air, which for efficiency reasons can be previously heated.
  • the present invention utilizes the separation of ballast injection into the furnace from the oxygen injection into the burner.
  • the flow of injected ballast (coming from the ratio of burner injection to boiler chamber injection) and the distribution of these injections will be different, depending on the desired effect.
  • one aspect of the present invention results in the smoothing, levelling or flattening of the flux profile on the walls of the burner.
  • the transfer profile corresponding to an oxygen flame has a non-uniform shape.
  • the main component of this transfer is radiation, owing to the high flame core temperature and above all the gases that predominantly make up the oxycombustion flue gases, namely CO 2 and H 2 O, radiating at high temperature.
  • the non-homogeneous temperature distribution along the length of the flame results in a non-uniform heat flux along the corresponding length of the furnace wall. This results in non-linear heat transfer issues, potential concerns about furnace wall (or tube wall) temperatures and other problems regarding localized excessive temperature concentrations.
  • the proposed way of making this flux more uniform is to inject the ballast along the side of the flame, along the side of the walls that would ordinarily be absorbing this heat, so as to effectively create a gas curtain.
  • This ballast gas curtain may contain gases that are not transparent to the radiation (i.e. CO 2 , H 2 O, coming for example from a flue gas recycle), and therefore absorb the radiation of the flame due to the fact of being comparatively cooler.
  • a greater ballast may be injected near the transfer peak to allow the height of the transfer peak to be reduced.
  • ballast gas may be injected with two operating positions (e.g. on/off), with the advantage of a simplified process and a simplified control scheme, and with the disadvantage of increased implementation complexity, potential flexibility issues, and the associated pressure drop through the system.
  • a lesser amount of ballast gas injection may incorporate a flow rate regulation in order to end up with the desired flux smoothing performance, with the advantage of greater control and more predictable results, and the disadvantage of a more complex process and a more complex control scheme.
  • ballast streams are injected vertically parallel with and substantially adjacent to the walls of the combustion chamber in a substantially downward direction. In one embodiment of the present invention the ballast streams are injected vertically parallel with and substantially adjacent to the walls of the combustion chamber in a substantially upward direction. In one embodiment of the present invention the ballast streams are injected horizontally parallel and substantially adjacent to the floor of the combustion chamber. In one embodiment of the present invention the ballast streams are injected horizontally parallel and substantially adjacent to the ceiling of the combustion chamber.
  • system data is provided to a control system, and the control system then controls the injection of the ballast streams. The system data may be fuel type, fuel characteristics, boiler operating conditions, exiting flue gas composition, or exiting flue gas temperature. Ballast injection streams rate and distribution can vary as well with boiler load.
  • sensors are mounted in the walls of the combustion chamber. These sensors provide input to a control system. The control system then controls the injection of the ballast streams.
  • the sensors may measure wall temperature, tube skin temperature, water wall fluid temperature, tube fluid temperature, furnace gas temperature, heat flux into the furnace wall, heat flux into the tubes or heat flux into the water walls.
  • ballast injection regulation is designed within this context on the flow rate and as a function of the flux measurements on the walls, but it may also take place as a function of the tube skin temperatures, or overall parameters such as the incoming power or the boiler combustion temperature outlet temperature, once the typical flux profile has been established for a combustion chamber configuration and a burner design.
  • a gaseous offset may also be produced.
  • This offset may be envisaged either for protecting the walls of the boiler from direct contact of the end of the flame (impingement) or for protecting them from lateral contact of the flame.
  • Direct contact of the flame on the walls has devastating effects on the integrity of the metal tubes that make up the walls of the chamber in usual boiler configurations. The points of possible impingement can be predicted in advance, thereby facilitating the arrangement of the injections into the boiler.
  • the ballast gas may be injected in parallel with the walls. This configuration may profit from the flux smoothing effect described above.
  • the ballast may be injected along the back wall of the furnace.
  • the ratio of ballast injected in the burners over the ballast injected into the furnace may depend on a number of operational criteria. This ratio may depend on the fuel characteristics. For example, with a difficult fuel (i.e. pitch difficult to atomize, wet fuels, fuels with a high content of incombustibles, fuels of a dangerous nature, etc.): the ballast injection ratio will be predominantly transferred towards the boiler, in order to allow and oxidant-rich combustion close to the burner. For a fuel with a high nitrogen content: to promote reaction mechanisms that reduce NOx formation, the ballast injection ratio will be displaced towards the burners, so as to create fuel-rich conditions at the flame.
  • a difficult fuel i.e. pitch difficult to atomize, wet fuels, fuels with a high content of incombustibles, fuels of a dangerous nature, etc.
  • the ballast injection ratio will be predominantly transferred towards the boiler, in order to allow and oxidant-rich combustion close to the burner.
  • the ballast injection ratio will
  • This ratio can also vary with boiler load, with a ratio displaced towards the boiler, in order to allow oxygen-rich conditions close to the burner to improve flame stability at low boiler load. Combined to this, the ratio may depend on operating conditions such as tube skin temperature, maximum flux measurement, and other operational criterial known to the skilled artisan.
  • FIG. 1 a schematic representation of the variation in heat flux experienced within the side walls of a furnace of a typical boiler as a function of flame profile.
  • FIG. 2 is a schematic representation of the variation in heat flux within the side walls of furnace of a typical boiler, as a function of flame profile, as modified by one embodiment of the present invention.
  • FIG. 3 is a schematic representation one aspect of the present invention.
  • the present invention is a method for injecting shielding gas into a boiler comprising;
  • shielding gas streams passing into a region of the combustion chamber a plurality of shielding gas streams, wherein the shielding gas streams are located, oriented, and controlled in a manner appropriate to protect an element in the region.
  • said region is selected from the group consisting of: the combustion chamber,
  • said element is selected from the group consisting of:
  • the shielding gas streams may be located, oriented, and controlled such that the shielding gas is injected vertically parallel with and substantially adjacent to the walls of the combustion chamber.
  • the shielding gas streams may be located, oriented, and controlled such that the shielding gas is injected vertically parallel with and substantially adjacent to the heat transfer elements positioned within the combustion chamber.
  • the ballast streams may be located, oriented, and controlled such that the shielding gas is injected horizontally parallel and substantially adjacent to the heat transfer elements positioned within the combustion chamber.
  • the ballast streams may be located, oriented, and controlled such that the shielding gas is injected horizontally parallel and substantially adjacent to the heat transfer elements positioned within the combustion chamber.
  • the shielding gas streams may be located, oriented, and controlled such that the shielding gas is injected vertically parallel with and substantially adjacent to one or more zones within the combustion chamber where the heat flux exceeds a predetermined value.
  • the shielding gas streams may be located, oriented, and controlled such that the shielding gas is injected in a direction substantially parallel to the direction of the combustion chamber jet.
  • the shielding gas streams may be located, oriented, and controlled such that the shielding gas is injected in a direction substantially perpendicular to the direction of the combustion chamber jet.
  • the shielding gas streams may be located, oriented, and controlled such that the shielding gas is injected in a direction substantially convergent to the direction of the combustion chamber jet.
  • the feeding ports for the shielding gas streams into the combustion chamber may be located more than 1 meter away from the burner jet.
  • the shielding gas streams may be injected such that at least one of the shielding gas streams has a swirl rate between 0.05 and 5, preferably between 0 . 26 and 1 . 73 .
  • This swirl rate is defined as I t over I a , I t and l a being respectively tangential and axial impulsions of the fluid rotated in the stream.
  • the present invention may further comprise
  • system data may be selected from the group consisting of:
  • ballast gas flows to the burners
  • the present invention may further comprise;
  • the sensors may measure a variable selected from the group consisting of wall temperature, tube skin temperature, water wall fluid temperature, tube fluid temperature, furnace gas temperature, and heat flux.
  • the shielding gas may comprise recycled flue gas.
  • the totality of injection of recycled flue gas into the boiler may be in the form of shielding gas.
  • the total injection of recycled flue gas into the boiler may be shared among ballast gas injected at the burners level and in the form of shielding gas.
  • the ballast gas injected at the burners level may be injected separately to an oxidant stream.
  • the ballast gas injected at the burners level may be injected after being mixed with an oxidant stream.
  • the shielding gas streams passing into the combustion chamber region may comprise at least one frequency with an amplitude of vibration, and wherein the boiler system comprises at least one natural frequency.
  • the ratio between the lowest frequency created by at least one of the shielding gas injections and the lowest natural frequency of the boiler system may be comprised between 0 and 0.95 or between 1.05 and 100, and preferably between 0 and 0.6 or between 1.3 and 5.
  • the flow of the different shielding gas injections may be controlled by the measure of the amplitude of the vibration at a location of the oxy-boiler selected from the group consisting of:
  • the shielding gas streams may have a controlled composition.
  • the shielding gas streams may have undergone a clean-up treatment before injection.
  • the shielding gas streams may have undergone a partial clean-up treatment before injection, aiming specifically at reducing the concentration of certain components.
  • the shielding gas streams may have undergone a partial clean-up treatment before injection, aiming specifically at reducing the concentration of corrosive components.
  • the shielding gas streams may have undergone a total or partial drying, so as to reduce the moisture content of these streams.
  • the shielding gas streams may be injected at temperatures between about ⁇ 50° C. to about 1500° C., preferably between about 100° C. and about 250° C.
  • the shielding gas streams may be injected at ambient temperature.
  • the shielding gas streams may have undergone thermal exchange against other fluids before injection.
  • the shielding gas streams may have undergone pre-heating before injection.
  • the shielding gas streams may be injected at different temperature levels at each injection point.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
US12/578,621 2008-10-24 2009-10-14 Method For Injecting Ballast Into An Oxycombustion Boiler Abandoned US20100101465A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP08167521.7 2008-10-24
EP08167521.7A EP2180252B1 (fr) 2008-10-24 2008-10-24 Procédé pour l'injection de ballast dans une chaudière à oxycombustion

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US20100101465A1 true US20100101465A1 (en) 2010-04-29

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US12/578,621 Abandoned US20100101465A1 (en) 2008-10-24 2009-10-14 Method For Injecting Ballast Into An Oxycombustion Boiler

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US (1) US20100101465A1 (fr)
EP (1) EP2180252B1 (fr)
WO (1) WO2010046296A1 (fr)

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RU2630625C1 (ru) * 2016-06-03 2017-09-11 Общество с ограниченной ответственностью научно-производственное предприятие "ИнтерПолярис" Способ образования газа в газогенераторе и газогенератор (варианты)

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US3048131A (en) * 1959-06-18 1962-08-07 Babcock & Wilcox Co Method for burning fuel
US3877440A (en) * 1974-01-18 1975-04-15 Foster Wheeler Corp Curtain air system for vapor generators
US4270467A (en) * 1980-01-14 1981-06-02 Enertherm, Inc. Low mass flow waste fuel incinerator
US4512266A (en) * 1983-03-30 1985-04-23 Kabushiki Kaisha Takuma City refuse incinerator for the prevention of clinker formation
US4656972A (en) * 1984-09-26 1987-04-14 Ishikawajima-Harima Jukogyo Kabushiki Kaisha Method and apparatus for reducing NOx in exhaust gases from fluidized-bed boiler
US5230868A (en) * 1989-04-04 1993-07-27 A. Ahlstrom Corporation Fluidized bed reactor with protected fluid distributor
US5044287A (en) * 1989-06-16 1991-09-03 Ebara Corporation Method of controlling combustion in a fluidized bed furnace
US5010827A (en) * 1990-05-08 1991-04-30 Wyerehaeuser Company Apparatus for detecting carryover particles in the interior of a furnace
US5632211A (en) * 1991-11-05 1997-05-27 Mitsubishi Jukogyo Kabushiki Kaisha Method and apparatus for waste incineration
US5368471A (en) * 1991-11-20 1994-11-29 The Babcock & Wilcox Company Method and apparatus for use in monitoring and controlling a black liquor recovery furnace
US5915310A (en) * 1995-07-27 1999-06-29 Consolidated Natural Gas Service Company Apparatus and method for NOx reduction by selective injection of natural gas jets in flue gas
US5626085A (en) * 1995-12-26 1997-05-06 Combustion Engineering, Inc. Control of staged combustion, low NOx firing systems with single or multiple levels of overfire air
US5807418A (en) * 1996-05-21 1998-09-15 Praxair Technology, Inc. Energy recovery in oxygen-fired glass melting furnaces
US5746144A (en) * 1996-06-03 1998-05-05 Duquesne Light Company Method and apparatus for nox reduction by upper furnace injection of coal water slurry
US5809913A (en) * 1996-10-15 1998-09-22 Cinergy Technology, Inc. Corrosion protection for utility boiler side walls
US5937772A (en) * 1997-07-30 1999-08-17 Institute Of Gas Technology Reburn process
US6422160B1 (en) * 1998-02-18 2002-07-23 Loesche Gmbh Apparatus for the combustion of vanadium-containing fuels
US6490985B2 (en) * 1998-08-20 2002-12-10 Hitachi, Ltd. Boiler
US6213032B1 (en) * 1999-08-30 2001-04-10 Energy Systems Associates Use of oil water emulsion as a reburn fuel
US6915751B1 (en) * 2000-02-18 2005-07-12 Niro A/S Method and apparatus for processing a pulverulent or particulate material
US6450108B2 (en) * 2000-03-24 2002-09-17 Praxair Technology, Inc. Fuel and waste fluid combustion system
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EP2180252B1 (fr) 2016-03-23
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