ES2118897T3 - Procedimiento para disminuir las emisiones de n2o de un reactor de lecho fluidizado. - Google Patents

Procedimiento para disminuir las emisiones de n2o de un reactor de lecho fluidizado.

Info

Publication number
ES2118897T3
ES2118897T3 ES93303984T ES93303984T ES2118897T3 ES 2118897 T3 ES2118897 T3 ES 2118897T3 ES 93303984 T ES93303984 T ES 93303984T ES 93303984 T ES93303984 T ES 93303984T ES 2118897 T3 ES2118897 T3 ES 2118897T3
Authority
ES
Spain
Prior art keywords
upper area
emissions
particular material
combustion
fluidized bed
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.)
Expired - Lifetime
Application number
ES93303984T
Other languages
English (en)
Inventor
Juan Antonio Garcia-Mallol
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.)
Foster Wheeler Energy Corp
Original Assignee
Foster Wheeler Energy Corp
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 Foster Wheeler Energy Corp filed Critical Foster Wheeler Energy Corp
Application granted granted Critical
Publication of ES2118897T3 publication Critical patent/ES2118897T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • 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 
    • F23C10/00—Fluidised bed combustion apparatus
    • F23C10/02—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed
    • F23C10/04—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone
    • F23C10/08—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases
    • F23C10/10—Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases the separation apparatus being located outside the combustion chamber
    • 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 
    • F23C6/00—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
    • F23C6/04—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
    • F23C6/045—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure
    • F23C6/047—Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection with staged combustion in a single enclosure with fuel supply in stages
    • 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 
    • F23C2206/00—Fluidised bed combustion
    • F23C2206/10—Circulating fluidised bed
    • F23C2206/101—Entrained or fast fluidised bed
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/10—Nitrogen; Compounds thereof
    • F23J2215/101—Nitrous oxide (N2O)

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Treating Waste Gases (AREA)

Abstract

LAS EMISIONES DE OXIDO NITROSO (N2O) SON REDUCIDAS EN UN REACTOR DE LECHO FLUIDIZADO UTILIZANDO COMBUSTION EN DOS ETAPAS. UNA ZONA INFERIOR DE LA SECCION DEL HORNO FUNCIONA BAJO CONDICIONES SUSTOIQUIOMETRICAS DE MODO QUE LA COMBUSTION EN LA ZONA INFERIOR ES INCOMPLETA, ASI SE INHIBE LA FORMACION DE N2O Y OXIDOS DE NITROGENO (NOX). UNA ZONA SUPERIOR DE LA SECCION DEL HORNO SE PONE EN FUNCIONAMIENTO BAJO CONDICIONES OXIDANTES PARA PROMOVER UNA COMBUSTION POSTERIOR. UNA CANTIDAD DE MATERIAL PARTICULAR ESTA PRESENTE EN LA ZONA SUPERIOR, Y ESTA CANTIDAD DE MATERIAL PARTICULAR EN LA ZONA SUPERIOR ES CONTROLADA PARA MANTENER UNA TEMPERATURA EN LA ZONA SUPERIOR PARA DESTRUIR EL N2O FORMADO DURANTE LA COMBUSTION. LA CANTIDAD DE MATERIAL PARTICULAR PRESENTE EN LA ZONA SUPERIOR PUEDE A SU VEZ SER CONTROLADA AL CONTROLAR EL MATERIAL PARTICULAR ENTRANTE A PARTIR DE LA ZONA INFERIOR HACIA LA ZONA SUPERIOR. LA TEMPERATURA ES TAMBIEN CONTROLADA PREFERENTEMENTE DENTRO DE UN PROMEDIO PARA PERMITIR LA CAPTURADE AZUFRE MEDIANTE PARTICULAS ABSORBENTES DE TAL FORMA QUE LAS EMISIONES DE N2O, NOX Y OXIDOS D AZUFRE (SOX) PUEDEN SER REDUCIDAS SIMULTANEAMENTE.
ES93303984T 1992-05-22 1993-05-21 Procedimiento para disminuir las emisiones de n2o de un reactor de lecho fluidizado. Expired - Lifetime ES2118897T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/886,892 US5325796A (en) 1992-05-22 1992-05-22 Process for decreasing N2 O emissions from a fluidized bed reactor

Publications (1)

Publication Number Publication Date
ES2118897T3 true ES2118897T3 (es) 1998-10-01

Family

ID=25390015

Family Applications (1)

Application Number Title Priority Date Filing Date
ES93303984T Expired - Lifetime ES2118897T3 (es) 1992-05-22 1993-05-21 Procedimiento para disminuir las emisiones de n2o de un reactor de lecho fluidizado.

Country Status (6)

Country Link
US (1) US5325796A (es)
EP (1) EP0571234B1 (es)
JP (1) JP2725133B2 (es)
KR (1) KR100272724B1 (es)
CA (1) CA2095486A1 (es)
ES (1) ES2118897T3 (es)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE502292C2 (sv) * 1994-08-19 1995-10-02 Kvaerner Enviropower Ab Förfarande för tvåstegsförbränning av fasta bränslen i en cirkulerande fluidiserad bädd
US5570645A (en) * 1995-02-06 1996-11-05 Foster Wheeler Energy Corporation Fluidized bed system and method of operating same utilizing an external heat exchanger
US5623822A (en) * 1995-05-23 1997-04-29 Montenay International Corp. Method of operating a waste-to-energy plant having a waste boiler and gas turbine cycle
ATE228225T1 (de) 1996-12-30 2002-12-15 Alstom Power Inc Verfahren zur kontrolle von stickoxiden bei einem dampferzeuger mit zirkulierender wirbelschicht
FI104793B (fi) * 1998-05-11 2000-04-14 Ahlstrom Machinery Oy Menetelmä typen oksidien poistamiseksi talteenottokattilan savukaasuista
FR2802287B1 (fr) * 1999-12-14 2002-01-11 Abb Alstom Power Comb Procede pour l'amelioration de la combustion dans un systeme a lit fluidise circulant et systeme correspondant
FI114737B (fi) * 2002-04-24 2004-12-15 Tom Blomberg Menetelmä biomassaa polttavien höyrykattiloiden höyrytulistimien asettelemiseksi ja höyrykattila
US20050072379A1 (en) * 2003-08-15 2005-04-07 Jupiter Oxygen Corporation Device and method for boiler superheat temperature control
JP5092114B2 (ja) * 2006-09-11 2012-12-05 中国電力株式会社 流動床ボイラにおける炭種切替に伴う流動媒体の炉内流動性管理方法
JP5435973B2 (ja) * 2009-01-30 2014-03-05 メタウォーター株式会社 流動焼却炉
FI123853B (fi) * 2009-03-06 2013-11-15 Metso Power Oy Menetelmä typenoksidipäästöjen vähentämiseksi happipoltossa
CN105588120B (zh) * 2016-03-02 2018-05-11 内蒙古金土环保科技有限公司 一种脱硫泛氧燃烧系统

Family Cites Families (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4039621A (en) * 1974-03-25 1977-08-02 Ralph M. Parsons Company Power generation wherein sulfur and nitrogen oxides are removed
JPS5239834A (en) * 1975-09-25 1977-03-28 Mitsubishi Heavy Ind Ltd Fluid bed combustion device
GB1523500A (en) * 1975-10-21 1978-09-06 Battelle Development Corp Method of operating a fluidized bed system
JPS53146326A (en) * 1977-05-27 1978-12-20 Daizou Kunii Method of preventing nox generation in fluid bed combustion
JPS5442868A (en) * 1977-09-09 1979-04-05 Ishikawajima Harima Heavy Ind Co Ltd Method of removing nitrogen oxide formed from fluid layer type waste matter incinerator
JPS5821163B2 (ja) * 1977-10-25 1983-04-27 川崎重工業株式会社 流動層の燃焼制御方法
JPS5832285B2 (ja) * 1977-11-25 1983-07-12 三井造船株式会社 含窒素可燃物の流動燃焼法
US4704084A (en) * 1979-12-26 1987-11-03 Battelle Development Corporation NOX reduction in multisolid fluidized bed combustors
US4308810A (en) * 1980-04-09 1982-01-05 Foster Wheeler Energy Corporation Apparatus and method for reduction of NOx emissions from a fluid bed combustion system through staged combustion
GB2095390B (en) * 1981-03-24 1984-11-21 Exxon Research Engineering Co Low pollution method of burning fuels
DE3447147A1 (de) * 1984-12-22 1986-06-26 Christian Dr.-Ing. 8570 Pegnitz Koch Verfahren und vorrichtung fuer die stickoxidfreie dampferzeugung mit fossilen brennstoffen
US4602573A (en) * 1985-02-22 1986-07-29 Combustion Engineering, Inc. Integrated process for gasifying and combusting a carbonaceous fuel
SE452359C (sv) * 1985-04-30 1994-04-11 Kvaerner Generator Ab Anordning för styrning av värmeövergångstalet vid en CFB-panna
US4809623A (en) * 1985-08-07 1989-03-07 Foster Wheeler Energy Corporation Fluidized bed reactor and method of operating same
US4809625A (en) * 1985-08-07 1989-03-07 Foster Wheeler Energy Corporation Method of operating a fluidized bed reactor
JPS62141408A (ja) * 1985-12-13 1987-06-24 Mitsubishi Heavy Ind Ltd 循環型流動床燃焼装置
JPH07101088B2 (ja) * 1986-01-22 1995-11-01 石川島播磨重工業株式会社 流動床炉の無触媒脱硝法
JPS6341708A (ja) * 1986-08-07 1988-02-23 Kawasaki Heavy Ind Ltd 流動燃焼法
JPS63279013A (ja) * 1987-05-07 1988-11-16 Ebara Corp 流動床焼却炉のＮＯ↓ｘ及び未燃ガス抑制装置
US4773339A (en) * 1987-05-15 1988-09-27 Foster Wheeler Energy Corporation Process for removing nitrous oxides from a gas
US5141708A (en) * 1987-12-21 1992-08-25 Foster Wheeler Energy Corporation Fluidized bed combustion system and method having an integrated recycle heat exchanger
JP2637449B2 (ja) * 1988-01-12 1997-08-06 三菱重工業株式会社 流動床燃焼方法
US4936770A (en) * 1988-11-25 1990-06-26 Foster Wheeler Energy Corporation Sulfur sorbent feed system for a fluidized bed reactor
US4955295A (en) * 1989-08-18 1990-09-11 Foster Wheeler Energy Corporation Method and system for controlling the backflow sealing efficiency and recycle rate in fluidized bed reactors
DE3933286A1 (de) * 1989-10-05 1991-04-18 Steinmueller Gmbh L & C Verfahren zur minderung des gehaltes an stickoxiden in den rauchgasen einer feuerung
JP2744666B2 (ja) * 1990-02-14 1998-04-28 三菱重工業株式会社 流動床燃焼炉内燃焼排ガス中の亜酸化窒素の低減方法
US5020456A (en) * 1990-02-28 1991-06-04 Institute Of Gas Technology Process and apparatus for emissions reduction from waste incineration

Also Published As

Publication number Publication date
JP2725133B2 (ja) 1998-03-09
US5325796A (en) 1994-07-05
EP0571234B1 (en) 1998-07-15
KR100272724B1 (ko) 2000-11-15
JPH0650510A (ja) 1994-02-22
EP0571234A2 (en) 1993-11-24
CA2095486A1 (en) 1993-11-23
KR930023058A (ko) 1993-12-18
EP0571234A3 (en) 1994-01-12

Similar Documents

Publication Publication Date Title
ES2118897T3 (es) Procedimiento para disminuir las emisiones de n2o de un reactor de lecho fluidizado.
CN105937766A (zh) 一种处理含氮废气、废液的低氮氧化物焚烧装置和方法
CN106969641A (zh) 一种烧结烟气自助燃分解二噁英脱硫脱硝回收余热系统及方法
MX9305448A (es) Reactor y metodo para la reduccion de emisores de oxido de azufre en un proceso de combustion.
CN111750670B (zh) 一种带还原炉与分解炉的分区组织燃烧自脱硝系统及工艺
SE8603035D0 (sv) Sett for nox-reduktion i mbc-pannor
ES2069660T3 (es) Procedimiento y dispositivo para reducir la concentracion de oxidos de nitrogeno en la corriente de gases de escape de procesos de combustion.
CA2036654A1 (en) Process and apparatus for reducing no_ emissions from combustion devices
ATE228225T1 (de) Verfahren zur kontrolle von stickoxiden bei einem dampferzeuger mit zirkulierender wirbelschicht
CN212440759U (zh) 一种适用于循环流化床锅炉全负荷脱硝控制系统
Leckner Influence of air supply on the emissions of NO and N2O from a circulating fluidized bed boiler
ES2009994A6 (es) Eliminacion del azufre mediante inyeccion de un material absorbente en zonas de combustion secundarias.
FI851188A0 (fi) Saett att vid eldning av fasta braenslen pao wanderrost minska utslaeppen av svavel- och kvaeveoxider.
CN2561497Y (zh) 煤粉炉内同时脱硫脱硝装置
CN2481976Y (zh) 低氮氧化物分解炉
JPS5450471A (en) Treating method for nitrogen oxides contained in exhaust gas
DK0476201T3 (da) Fremgangsmåde til styring af emissioner af sur gas i forbrændingsgasser fra kraftværker
CN1387939A (zh) 煤粉炉内同时脱硫脱硝方法及装置
JPS52101663A (en) Treatment of nitrogen oxides of high concentration
JPS5668713A (en) Fluidized incinerator for mixed combustion of coal and refuse
JPS59205507A (ja) 微粉炭の炉内脱硝燃焼装置
JPS5620915A (en) Method of controlling combustion in fluidized incinerator
Khan et al. Effect of staged combustion on in-situ desulphurization by limestone in a fluidised bed combustor
JPH0368286B2 (es)
JPS54123737A (en) Method of burning with small amount of nitrogen oxide product

Legal Events

Date Code Title Description
FG2A Definitive protection

Ref document number: 571234

Country of ref document: ES