EP0434945A2 - Wirbelschichtmüllverbrennungsanlage - Google Patents

Wirbelschichtmüllverbrennungsanlage Download PDF

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Publication number
EP0434945A2
EP0434945A2 EP90121485A EP90121485A EP0434945A2 EP 0434945 A2 EP0434945 A2 EP 0434945A2 EP 90121485 A EP90121485 A EP 90121485A EP 90121485 A EP90121485 A EP 90121485A EP 0434945 A2 EP0434945 A2 EP 0434945A2
Authority
EP
European Patent Office
Prior art keywords
fluid
hearth
delivery duct
combustion chamber
bed incinerator
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.)
Granted
Application number
EP90121485A
Other languages
English (en)
French (fr)
Other versions
EP0434945B1 (de
EP0434945A3 (en
Inventor
Piergiorgio Fontana
Sergio Zuccotti
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.)
Italimpianti SpA
Original Assignee
Italimpianti SpA
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 Italimpianti SpA filed Critical Italimpianti SpA
Publication of EP0434945A2 publication Critical patent/EP0434945A2/de
Publication of EP0434945A3 publication Critical patent/EP0434945A3/en
Application granted granted Critical
Publication of EP0434945B1 publication Critical patent/EP0434945B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/006—Layout of treatment plant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B31/00—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements or dispositions of combustion apparatus
    • F22B31/0007—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements or dispositions of combustion apparatus with combustion in a fluidized bed
    • F22B31/0084—Modifications of boiler construction, or of tube systems, dependent on installation of combustion apparatus; Arrangements or dispositions of combustion apparatus with combustion in a fluidized bed with recirculation of separated solids or with cooling of the bed particles outside the combustion bed
    • 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
    • F23C10/18—Details; Accessories
    • F23C10/20—Inlets for fluidisation air, e.g. grids; Bottoms
    • 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
    • F23C10/18—Details; Accessories
    • F23C10/24—Devices for removal of material from the bed
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/30—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a 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 
    • F23J7/00—Arrangement of devices for supplying chemicals to fire
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2217/00—Intercepting solids
    • F23J2217/10—Intercepting solids by filters
    • F23J2217/101—Baghouse type
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2219/00—Treatment devices
    • F23J2219/70—Condensing contaminants with coolers

Definitions

  • the object of the invention is a fluid-bed incinerator comprising a kiln with its combustion chamber being formed with a gas-pervious hearth, and which is provided with means for loading into the combustion chamber any refuse to be incinerated above the hearth, and with means for feeding through the gas-pervious hearth an upward combustion air flow, and also with means for feeding reagents into the combustion chamber.
  • the object of the invention is to provide a fluid-bed incinerator of the type as described at the outset, which is of a simple, relatively not expensive construction, and at the same time guarantees such optimum conditions in the fluid bed that a perfect course of the combustion process will be obtained.
  • the invention attains this object by the provision of a fluid-bed incinerator of the type as described at the outset, with the hearth of the combustion chamber in the kiln being formed with a centrally located outlet opening which is connected to a delivery duct, means being provided for feeding cold air into the combustion chamber, through the delivery duct and the outlet opening in the hearth.
  • the outlet opening in the hearth is preferably fitted with a tubular hub which is connected to a delivery duct consisting of a first delivery duct and a successive, second delivery duct, and which is received into the counterbored upward end of the first delivery duct, the free downward end of the first delivery duct extending into the interior of a widened portion in the successive, second delivery duct.
  • a cold air feeding duct is provided, which opens into the counterbored end of the first delivery duct, preferably at a higher level than the lower end of this hub, and a cold air suction duct is provided, which is connected with the widened portion in the successive delivery duct, preferably above the downward free end of the first delivery duct.
  • the cold air feeding and suction means are so provided that the fed cold air flow is parted into an upward cold air flow flowing into the combustion chamber in the kiln at a flow rate of 75% of the fed cold air flow, and into a cold air downward flow drawn into the suction means at a flow rate of 25% of the fed cold air flow.
  • cold air renders it possible to have the residual products of combustion cooled, generally from a temperature of about 850°C down to a temperature of about 200-70°C.
  • the fine particle size material forming the mass of the fluid bed is efficiently separated from the said residual products of combustion owing to the said material being upwardly entrained in the fluid bed.
  • the air that cools the residual products of combustion also allows a certain energy recovery therefrom. This air actually is in a degree of from 10 to 20% of the total air for the fluid-bed process, the combustion air for the incinerating process.
  • a further feature of the invention resides in that reagents having a fine particle size of about 100 micromillimeters, which in any case is such as to allow the reagents to be partly or entirely drawn along with the flue gases, are preferably fed pneumatically into the combustion chamber, in the inside of the fluid bed, and/or over the fluid bed itself.
  • the ashes of the burned refuse will have their softening temperature increased of about 200°C, particularly owing to the action of carbonates, oxides, and hydroxides of alkaline-earth metals, whereby the forming of any agglomerate in the fluid bed, on the surfaces of the fluid-bed-cooling tube nest, on the combustion chamber refractory walls, and around an auxiliary burner which may be provided for a successive flue gas post-heating, is at the same time avoided.
  • a part of the flue gas-entrained "fresh" chemical reagents is also caused to get into the bag filter at a temperature of 110-150°C, whereby the acid gases cast-down reaction is completed.
  • the fluid-bed incinerator equipment comprises a kiln 1.
  • the hot gases used for pre-heating the mass of the fluid bed at the time the incinerator is being started are produced in a generator 2 fitted with a burner 3.
  • the hot gases and the combustion air are fed underneath the hearth 6 of the combustion chamber in kiln 1, into two annular chambers 7 and 8.
  • the hearth 6 is made in form of a conical hopper, and is gas-pervious.
  • the kiln 1 is fitted at its bottom area with a duct 9 for delivering the residual products of combustion, which by its top end is connected with a centrally located outlet opening 106 in hearth 6, and by its lower end opens into a vessel 10 for collection of the residual products of combustion. Any particulate matter being entrained by the flue gases to the exterior of the fluid bed, is fed to a cyclone 11 in which most of the entrained dusts are separated from the flue gases.
  • the collected dusts are then delivered into a dust-collecting container 12, or the same are again conveyed into the kiln 1 of the fluid-bed incinerator, while the flue gases containing any residual dusts with a very fine particle size, are introduced into a successive, secondary combustion chamber 13 fitted with a burner 14.
  • the flue gases are then fed to a fume cooler 16.
  • the outlet of the fume cooler 16 is connected to a successive bag filter 17, in which any dusts contained in the flue gases are separated therefrom and delivered into a dust-collecting container 18, while with the aid of an exhauster fan 20, the dust-freed flue gases are vented into the atmosphere through a stack 19.
  • any refuse to be incinerated is loaded into the combustion chamber preferably over the fluid-bed surface S, by suitable refuse-loading means designated by numeral 21.
  • Numeral 22 denotes the reagent feeding means. Reagents are fed into the fluid bed, and/ or are fed at such a level thereover, and are of such a particle size that an optimum, reagent-dwelling time within the furnace is achieved, and that the reagents can be then drawn along with the flue gases. Thanks to such a procedure, a good reagent-neutralizing reaction with acid gases, such as HCL, SO2, HBR, HF, HCN, is ensured not only in the fluid bed, but also in the region over the fluid bed surface S.
  • acid gases such as HCL, SO2, HBR, HF, HCN
  • the used reagents may be of different-types, and, for example, Ca(OH)2, Mg(OH)2, CaO, MgO, CaCO3, MgCO3, Na2CO3 are preferably used.
  • the ashes of the burned refuse will have their softening temperature increased up to about 200°, particularly owing to the action of carbonates, oxides, and hydroxides of alkaline-earth metals, whereby the forming of any agglomerate is avoided in the fluid bed, on the fluid-bed-cooling tube nest, on the refractory walls of the kiln, and in proximity of the auxiliary, flue gas post-heating burner 14.
  • the hearth 6 of the combustion chamber in kiln 1 of the fluid-bed incinerator is, according to the invention, made in form of a gas-pervious conical hopper.
  • the hearth 6 is formed with a centrally located outlet opening 106 which is connected with a downwardly directed tubular hub 23.
  • the tubular hub 23 is fitted into a delivery duct 9 consisting of a first delivery duct 24, and of a successive, second delivery duct 25, and is received into the counterbored upper end 124 of the first delivery duct 24, the downward free end of the first delivery duct 24 being in turn received into a widened portion 125 in the successive, second delivery duct 25.
  • annular chamber T1 is formed, with a cold air feeding duct 26 opening thereinto.
  • Cold air flows into the combustion chamber in kiln 1 through the tubular hub 23 and the associated opening 106, and causes the residual products of combustion to be cooled.
  • a certain energy recovery from the residual products of combustion is also obtained, in that the air that cools the residual products of combustion, forms in a degree of 10 to 20%, a part of the combustion air for the combustion process.
  • a better separation of the residual products of combustion from the fine particle size material forming the fluid bed is achieved, owing to this fine particle size material being upwardly entrained.
  • the cold air feeding duct 26 preferably opens into the annular chamber T1 at a slightly higher level than the opening at the downward free end of the tubular hub 23, and a suction duct 27 opens into the widened portion 125 in the delivery duct 25, that is, into the annular chamber T2 formed between the said widened portion and the lower end section of the first delivery duct 24.
  • the mouth of suction duct 27 also lies preferably at a higher level than the opening at the downward free end of the first delivery duct 24.
  • the cold air flow fed into the annular chamber T1 is parted into two partial flows, that is, an upward partial cold air flow flowing into the combustion chamber in kiln 1 through the opening 106 in the hearth 6 of said kiln 1, and a downward cold air partial flow which is associated with the residual products of combustion, and is drawn into the suction duct 27.
  • the upward cold air partial flow preferably is about 75% of the fed, total cold air flow, while the downward cold air partial flow is formed by the remaining 25% of the fed cold air flow.
  • the cold air suction duct 27 feeds cold air to the bag filter, in which the cold air is dust-freed, and together with the purified flue gases is then vented into the atmosphere.
  • the hearth 6 of the combustion chamber in kiln 1 is gas-pervious, thanks to the provision of a plurality of spaced apart through bores 206 made in the whole extent thereof.
  • a lamina 28 for holding back this sand-like matter is provided at a distance below each bore 206.
  • the laminae 28 may be made in any suitable manner and, for example, they may consist of substantially Z-shaped platelets which by one of their horizontal arms are secured to the underside of hearth 6.
  • the diameter of these through bores preferably is of about 7 mm, and the hearth must be given an inclination of at least 15°, in order to ensure an efficient downflow of the residual products of combustion through the outlet opening 106.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Crucibles And Fluidized-Bed Furnaces (AREA)
  • Incineration Of Waste (AREA)
EP90121485A 1989-12-28 1990-11-09 Wirbelschichtmüllverbrennungsanlage Expired - Lifetime EP0434945B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT01262189A IT1236182B (it) 1989-12-28 1989-12-28 Forno d'incenerimento a letto fluido.
IT1262189 1989-12-28

Publications (3)

Publication Number Publication Date
EP0434945A2 true EP0434945A2 (de) 1991-07-03
EP0434945A3 EP0434945A3 (en) 1992-05-27
EP0434945B1 EP0434945B1 (de) 1994-12-28

Family

ID=11142281

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90121485A Expired - Lifetime EP0434945B1 (de) 1989-12-28 1990-11-09 Wirbelschichtmüllverbrennungsanlage

Country Status (4)

Country Link
EP (1) EP0434945B1 (de)
AT (1) ATE116420T1 (de)
DE (1) DE69015601T2 (de)
IT (1) IT1236182B (de)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0717260A3 (de) * 1994-12-15 1996-10-23 Buck Chem Tech Werke Verfahren zur Aufarbeitung von pyrotechnischem Material
EP0999412A4 (de) * 1997-03-13 2001-01-03 Hitachi Shipbuilding Eng Co Verbrennungsvorrichtung
BE1015530A3 (nl) * 2003-05-20 2005-05-03 Fifth Element Nv Verbeterde inrichting voor het realiseren van een wervelbed.

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE793489A (fr) * 1972-03-06 1973-04-16 Awt Systems Inc Appareil ameliore a lit fluidise
GB1577717A (en) * 1976-03-12 1980-10-29 Mitchell D A Thermal reactors incorporating fluidised beds
US4308806A (en) * 1978-04-05 1982-01-05 Babcock-Hitachi Kabushiki Kaisha Incinerator for burning waste and a method of utilizing same
JPS5866712A (ja) * 1981-10-16 1983-04-21 Nippon Zeon Co Ltd 流動焼却炉付帯設備の腐食防止法
FR2583305B1 (fr) * 1985-06-18 1989-10-27 Fives Cail Babcock Procede de desulfuration des gaz provenant du foyer d'une chaudiere et installation pour la mise en oeuvre de ce procede.
US4854249A (en) * 1987-08-03 1989-08-08 Institute Of Gas Technology Two stage combustion

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0717260A3 (de) * 1994-12-15 1996-10-23 Buck Chem Tech Werke Verfahren zur Aufarbeitung von pyrotechnischem Material
EP0999412A4 (de) * 1997-03-13 2001-01-03 Hitachi Shipbuilding Eng Co Verbrennungsvorrichtung
US6264465B1 (en) 1997-03-13 2001-07-24 Hitachi Zosen Corporation Combustion device
BE1015530A3 (nl) * 2003-05-20 2005-05-03 Fifth Element Nv Verbeterde inrichting voor het realiseren van een wervelbed.

Also Published As

Publication number Publication date
IT1236182B (it) 1993-01-19
EP0434945B1 (de) 1994-12-28
IT8912621A1 (it) 1991-06-28
DE69015601D1 (de) 1995-02-09
DE69015601T2 (de) 1995-05-11
ATE116420T1 (de) 1995-01-15
IT8912621A0 (it) 1989-12-28
EP0434945A3 (en) 1992-05-27

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