SE7609676L - DEVICE FOR COMBUSTION OF CARBONIC SUBSTANCE - Google Patents

DEVICE FOR COMBUSTION OF CARBONIC SUBSTANCE

Info

Publication number
SE7609676L
SE7609676L SE7609676A SE7609676A SE7609676L SE 7609676 L SE7609676 L SE 7609676L SE 7609676 A SE7609676 A SE 7609676A SE 7609676 A SE7609676 A SE 7609676A SE 7609676 L SE7609676 L SE 7609676L
Authority
SE
Sweden
Prior art keywords
fluidized
inlet
combustion
bed
gas
Prior art date
Application number
SE7609676A
Other languages
Unknown language ( )
Swedish (sv)
Other versions
SE424225B (en
SE424225C (en
Inventor
L Reh
M Hirsch
P H Collin
S N Flink
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 SE7609676L publication Critical patent/SE7609676L/en
Publication of SE424225B publication Critical patent/SE424225B/en
Publication of SE424225C publication Critical patent/SE424225C/en

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

1510946 Fluidized-bed combustion METALLGES AG 9 July 1976 [5 Sept 1975] 28750/76 Heading F4B A process for combustion under approximately stoichiometric conditions in which carbonaceous material is fed through a lance 7 to a fluidized-bed reactor 1 which is fluidizedby gas supplied through an inlet 8 and by a secondary gas supplied through an inlet 2 or which can be supplied at a plurality of superimposed levels (2a-2d), Fig. 2 (not shown). At least the secondary gas contains oxygen for the combustion of the carbonaceous material in the fluidized bed. The volume ratio of fluidizing gas supplied at 8 to secondary gas supplied at 2 is in the range from 1 : 20 to 2 : 1 and the two gas supplies are adjusted so that suspension density of the fluidized bed above the inlet 2 level is in the range 15 to 100 Kg/M<SP>3</SP>. Solids entrained by the exhaust gas from the fluidized-bed are collected in the separator 6 and are recycled through a conduit 9 back into the reactor 1. Surplus solids produced are withdrawn through a conduit 10. Part of the heat of combustion is dissipated through cooling surfaces 3 in the space above the inlet 2 level. Other heat heat exchange surfaces may be located at positions 4 and 5 in the reactor and separator. Solids discharged from the conduit 10 may be fed to a fluidized-bed cooler 14, which is fluidized by oxygen containing gas which is then fed to the inlet 2. The cooler 14 has cooling registers 13 in which solids are cooled indirectly by gas supplied through a conduit 17 and later fed as fluidizing gas to the inlet 8. Part of this gas supply may be used for pneumatically feeding the carbonaceous material through the lance 7. The combustion process may be carried out under superatmospheric pressure.
SE7609676A 1975-09-05 1976-09-01 PROCEDURE NEEDS NEAR STOCHIOMETRIC PRESENTATION OF CARBONIC SUBSTANCES IN SPIRIT LAYERS SE424225C (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 (3)

Publication Number Publication Date
SE7609676L true SE7609676L (en) 1977-03-06
SE424225B SE424225B (en) 1982-07-05
SE424225C SE424225C (en) 1990-08-30

Family

ID=5955703

Family Applications (1)

Application Number Title Priority Date Filing Date
SE7609676A SE424225C (en) 1975-09-05 1976-09-01 PROCEDURE NEEDS NEAR STOCHIOMETRIC PRESENTATION OF CARBONIC SUBSTANCES IN SPIRIT LAYERS

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.
DE3688007D1 (en) 1985-06-12 1993-04-22 Metallgesellschaft Ag COMBUSTION DEVICE WITH CIRCULATING FLUID BED.
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
US6418866B1 (en) 1998-06-16 2002-07-16 Mitsubishi Heavy Industries, Ltd. Operating method of fluidized-bed incinerator and the incinerator

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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
NL113541C (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
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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
CS212255B2 (en) 1982-03-26
SE424225B (en) 1982-07-05
AU1572476A (en) 1978-01-12
AU500206B2 (en) 1979-05-10
FR2323101B1 (en) 1982-10-01
DD126526A5 (en) 1977-07-20
RO86704B (en) 1985-05-01
IN143376B (en) 1977-11-12
ES451239A1 (en) 1977-09-16
GB1510946A (en) 1978-05-17
ZA763293B (en) 1977-05-25
RO86704A (en) 1985-04-17
DE2539546A1 (en) 1977-03-17
SU898960A3 (en) 1982-01-15
FR2323101A1 (en) 1977-04-01
JPS5233132A (en) 1977-03-14
BE845872A (en) 1977-03-03
DE2539546B2 (en) 1980-11-27
CA1057584A (en) 1979-07-03
DE2539546C3 (en) 1985-10-24
JPS5728046B2 (en) 1982-06-14
SE424225C (en) 1990-08-30

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