ES451239A1 - Process for burning carbonaceous materials - Google Patents

Process for burning carbonaceous materials

Info

Publication number
ES451239A1
ES451239A1 ES451239A ES451239A ES451239A1 ES 451239 A1 ES451239 A1 ES 451239A1 ES 451239 A ES451239 A ES 451239A ES 451239 A ES451239 A ES 451239A ES 451239 A1 ES451239 A1 ES 451239A1
Authority
ES
Spain
Prior art keywords
secondary gas
gas
combustion
fluidized layer
point
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
Application number
ES451239A
Other languages
Spanish (es)
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.)
GEA Group AG
Original Assignee
Metallgesellschaft AG
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 Metallgesellschaft AG filed Critical Metallgesellschaft AG
Publication of ES451239A1 publication Critical patent/ES451239A1/en
Expired 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
    • B01J8/38—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 with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—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 with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388—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 with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • 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 
    • F23C2206/00—Fluidised bed combustion
    • F23C2206/10—Circulating fluidised bed
    • F23C2206/101—Entrained or fast fluidised bed
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

Procedure for the almost stoichiometric combustion of carbonaceous materials in the fluidized layer, with return of the discharged solids to the fluidized layer, evacuation of the combustion heat by means of cooling surfaces, characterized in that combustion is carried out with two partial streams of oxygenated gases fed at different heights, of which at least one is incorporated as a secondary gas in one or more superimposed planes; because the volumetric ratio between fluidization gas and secondary gas is adjusted to a value in the range of 1:20 to 2: 1; Because above the feed point of the secondary gas, and by adjusting the gas velocity and the ratio of fluidizing gas to secondary gas, a state of the fluidized layer with an average suspension density of 15 to 100 kg/m3; because at least a substantial part of the heat of combustion is evacuated by means of cooling surfaces located in the free space of the furnace above the point of supply of the secondary gas: because the preponderant part of the carbon material is loaded into the space practically free of internal structures, located below the secondary gas supply point, and because the solids are taken from the circulation system formed by the fluidized layer reactor, the separator and the return line. (Machine-translation by Google Translate, not legally binding)
ES451239A 1975-09-05 1976-09-03 Process for burning carbonaceous materials Expired ES451239A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2539546A DE2539546C3 (en) 1975-09-05 1975-09-05 Process for incinerating carbonaceous materials

Publications (1)

Publication Number Publication Date
ES451239A1 true ES451239A1 (en) 1977-09-16

Family

ID=5955703

Family Applications (1)

Application Number Title Priority Date Filing Date
ES451239A Expired ES451239A1 (en) 1975-09-05 1976-09-03 Process for burning carbonaceous materials

Country Status (15)

Country Link
JP (1) JPS5233132A (en)
AU (1) AU500206B2 (en)
BE (1) BE845872A (en)
CA (1) CA1057584A (en)
CS (1) CS212255B2 (en)
DD (1) DD126526A5 (en)
DE (1) DE2539546C3 (en)
ES (1) ES451239A1 (en)
FR (1) FR2323101A1 (en)
GB (1) GB1510946A (en)
IN (1) IN143376B (en)
RO (1) RO86704B (en)
SE (1) SE424225C (en)
SU (1) SU898960A3 (en)
ZA (1) ZA763293B (en)

Families Citing this family (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2624302A1 (en) * 1976-05-31 1977-12-22 Metallgesellschaft Ag PROCEDURE FOR CARRYING OUT EXOTHERMAL PROCESSES
SE421723B (en) * 1977-05-09 1982-01-25 Goetaverken Angteknik Ab SET AND REACTOR FOR PERFORMANCE OF EXOTERMA REACTIONS, INCLUDING COMBUSTION, IN A CIRCULATED FLOAT BED
JPS54108023A (en) * 1978-02-10 1979-08-24 Mitsubishi Mining & Cement Co Method of burning solid fuel and its device
GB1604999A (en) * 1978-05-31 1981-12-16 Deborah Fluidised Combustion Boilers
DK155464C (en) * 1978-10-27 1989-08-21 Smidth & Co As F L WHIRL CHAMBER BRANCH SYSTEM
CH636942A5 (en) * 1979-05-30 1983-06-30 Sulzer Ag Fluidized bed firing with a flat grate.
CH651644A5 (en) * 1980-11-13 1985-09-30 Sulzer Ag COOLED COMBUSTION ROOM WITH A FLUIDIZED BURN COMBUSTION AND METHOD FOR OPERATING THE SAME.
DE3107355C2 (en) * 1981-02-27 1990-11-15 L. & C. Steinmüller GmbH, 5270 Gummersbach Process for producing a fluidized bed with fluidized bed mass regulation
FI66297C (en) * 1982-11-15 1984-10-10 Ahlstroem Oy ANORDINATION FOR AVAILABLE FASHION COMPONENTS FOR ROVERGASER
US4453497A (en) * 1982-12-21 1984-06-12 Struthers Wells Corporation Augmented heat transfer method and apparatus
DE3306795C1 (en) * 1983-02-26 1983-12-15 L. & C. Steinmüller GmbH, 5270 Gummersbach Process for binding sulfur compounds, which are formed as reaction products when burning sulfur-containing fuels in a furnace by adding additives
NL8302112A (en) * 1983-06-14 1985-01-02 Tno METHOD AND APPARATUS FOR BURNING A FUEL USING A FLUIDIZED BED.
DE3347083A1 (en) * 1983-12-24 1985-07-04 Vereinigte Kesselwerke AG, 4000 Düsseldorf Immersion heating surfaces for a fluidised-bed furnace
DE3431343A1 (en) * 1983-12-24 1986-03-06 Vereinigte Kesselwerke AG, 4000 Düsseldorf Immersion-heating surfaces for fluidised-bed firing
FR2560967B1 (en) * 1984-03-08 1988-08-26 Creusot Loire METHOD AND APPARATUS FOR CONTROLLING THE THERMAL TRANSFER CARRIED OUT IN A FLUIDIZED BED
FI79403C (en) * 1984-06-01 1989-12-11 Ahlstroem Oy FOERBRAENNINGSMETOD.
ATE87077T1 (en) 1985-06-12 1993-04-15 Metallgesellschaft Ag CIRCULATION FLUID BED COMBUSTER.
DE3544425A1 (en) * 1985-12-16 1987-06-25 Steag Ag METHOD FOR BURNING SOLID FUELS IN A CIRCULATING FLUID BED, AND DEVICE FOR CARRYING OUT THIS METHOD
DE3605930A1 (en) * 1986-02-25 1987-08-27 Steinmueller Gmbh L & C Process for burning carbon-containing fuels in a circulating fluidised bed and apparatus for carrying out the process
DE3621593C1 (en) * 1986-06-27 1988-01-21 Prof Dr Bohn Thomas J Fluidised-bed reactor, in particular for a fluidised-bed furnace
DE3625992A1 (en) * 1986-07-31 1988-02-04 Steinmueller Gmbh L & C METHOD FOR BURNING CARBON-CONTAINING MATERIALS IN A CIRCULATING FLUID BED, AND A FLUET BURNING PLANT FOR CARRYING OUT THE METHOD
DE3706538A1 (en) * 1987-02-28 1988-09-08 Metallgesellschaft Ag Fluidized bed system
DE3708799A1 (en) * 1987-03-18 1988-09-29 Steinmueller Gmbh L & C METHOD FOR BURNING CARBON-CONTAINING MATERIAL IN A FLUIDIZED BURNER AND APPARATUS FOR CARRYING OUT THE METHOD
FR2620517B1 (en) * 1987-09-14 1989-12-22 Fives Cail Babcock FLUIDIZED BED COMBUSTION PROCESS AND INSTALLATION FOR CARRYING OUT SAID METHOD
IN170802B (en) * 1988-06-25 1992-05-23 Metallgesellschaft Ag
DE3921076C1 (en) * 1989-06-28 1991-02-07 Vereinigte Kesselwerke Ag, 4000 Duesseldorf, De
DE3929178A1 (en) * 1989-09-02 1991-03-21 Balcke Duerr Ag FLUIDIZED LAYER REACTOR AND RELATED OPERATING METHOD
DE4005305A1 (en) * 1990-02-20 1991-08-22 Metallgesellschaft Ag FLUIDIZED LAYER REACTOR
FR2661113B1 (en) * 1990-04-20 1993-02-19 Stein Industrie DEVICE FOR PERFORMING A REACTION BETWEEN A GAS AND A SOLID MATERIAL DIVIDED IN AN ENCLOSURE.
TR26264A (en) * 1991-05-02 1995-02-15 Stein Industrie A GAS AND A GAS IN A CLOSED VENUE AND MORE THAT ARE GOOD TO REACT.
DE4202895C2 (en) * 1992-02-01 1997-09-18 Preussag Noell Gmbh Device for burning carbonaceous fuels in a circulating fluidized bed
EP1013994A4 (en) 1998-06-16 2003-01-02 Mitsubishi Heavy Ind Ltd Operating method of fluidized-bed incinerator and the incinerator

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL73332C (en) * 1940-01-03 1950-07-15
US2416462A (en) * 1942-11-12 1947-02-25 Babcock & Wilcox Co Method of and apparatus for recovering heat and chemicals
FR1112407A (en) * 1953-09-15 1956-03-14 Basf Ag Process for the combustion of carbonaceous materials and the recovery of the heat of combustion
GB784595A (en) * 1954-08-05 1957-10-09 Combustion Eng Improvements in vapour, e.g. steam generation
GB776791A (en) * 1954-09-09 1957-06-12 Basf Ag Apparatus for steam production
US2842102A (en) * 1954-11-18 1958-07-08 Combustion Eng Steam generation
DE966644C (en) * 1956-07-02 1957-08-29 Basf Ag Process for operating hot gas turbines
NL113546C (en) * 1958-03-24
DE1159120B (en) * 1958-04-03 1963-12-12 Basf Ag Fluidized bed combustion for multi-stage combustion of fine-grain fuel
US3050202A (en) * 1958-11-18 1962-08-21 Combustion Eng Bark-type fuel feeder with vibrating proportioning table and flow dividing means
GB1203755A (en) * 1966-10-27 1970-09-03 Coal Industry Patents Ltd Method of and apparatus for generating heat
GB1143880A (en) * 1967-06-16 1900-01-01
DE1767628C3 (en) * 1968-05-30 1985-03-14 Metallgesellschaft Ag, 6000 Frankfurt Process for performing endothermic processes
US3508506A (en) * 1968-06-13 1970-04-28 Us Interior Process and apparatus for reduction of unburned combustible in fly ash
US3513813A (en) * 1968-12-31 1970-05-26 Us Interior Dilute phase particulate matter reactor-heat exchanger
US3625164A (en) * 1971-04-21 1971-12-07 Air Prod & Chem Combustion of high-sulfur coal in a fluidized bed reactor
US3863577A (en) * 1971-11-22 1975-02-04 Dorr Oliver Inc Fluidized bed reactor
US3763830A (en) * 1973-01-24 1973-10-09 Us Interior Apparatus for burning sulfur containing fuels
US3884193A (en) * 1974-03-22 1975-05-20 Foster Wheeler Corp Vapor generating system and method

Also Published As

Publication number Publication date
AU500206B2 (en) 1979-05-10
SE7609676L (en) 1977-03-06
IN143376B (en) 1977-11-12
JPS5233132A (en) 1977-03-14
SE424225B (en) 1982-07-05
JPS5728046B2 (en) 1982-06-14
RO86704A (en) 1985-04-17
GB1510946A (en) 1978-05-17
SE424225C (en) 1990-09-10
RO86704B (en) 1985-05-01
CA1057584A (en) 1979-07-03
DE2539546B2 (en) 1980-11-27
FR2323101B1 (en) 1982-10-01
FR2323101A1 (en) 1977-04-01
AU1572476A (en) 1978-01-12
ZA763293B (en) 1977-05-25
CS212255B2 (en) 1982-03-26
SU898960A3 (en) 1982-01-15
DE2539546C3 (en) 1985-10-24
DD126526A5 (en) 1977-07-20
BE845872A (en) 1977-03-03
DE2539546A1 (en) 1977-03-17

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