EP0362348A1 - Appareil de combustion pour bruler des combustibles solides - Google Patents
Appareil de combustion pour bruler des combustibles solidesInfo
- Publication number
- EP0362348A1 EP0362348A1 EP19890904036 EP89904036A EP0362348A1 EP 0362348 A1 EP0362348 A1 EP 0362348A1 EP 19890904036 EP19890904036 EP 19890904036 EP 89904036 A EP89904036 A EP 89904036A EP 0362348 A1 EP0362348 A1 EP 0362348A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- combustion
- combustion chamber
- firing device
- chamber
- grate
- 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.)
- Withdrawn
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23B—METHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
- F23B90/00—Combustion methods not related to a particular type of apparatus
- F23B90/04—Combustion methods not related to a particular type of apparatus including secondary combustion
- F23B90/06—Combustion methods not related to a particular type of apparatus including secondary combustion the primary combustion being a gasification or pyrolysis in a reductive atmosphere
-
- 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
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
Definitions
- the invention relates to a firing device for the combustion of solid fuels, in particular for the combustion of waste materials.
- This object is achieved according to the invention in that a primary combustion device which receives the solid fuels and causes their gasification is followed by a separate secondary combustion device for burning the fuels present in the gaseous state, the secondary combustion device preferably being a combustion gas chamber connected to the combustion chamber of the primary combustion device as well as an adjoining main combustion chamber.
- the already partially burning gases coming from the primary combustion devices, the secondary combustion air quantities necessary for the secondary combustion and, if necessary, a recycle exhaust gas quantity which is favorable for NOx reduction can be mixed in and thus achieve an optimal one Burnout mixture are prepared. Thereafter, the processed fuel gases flow into the main combustion chamber of the secondary combustion device, where they can burn out completely at moderate flow speeds and balanced temperatures.
- the fuel gases are supplied with the necessary secondary combustion air and, if necessary, with other gases, e.g., before entering the combustion chamber of the secondary combustion device.
- the combustion chamber described is closed at the top and has an outlet opening arranged offset to the inlet opening.
- a combustor shaft is arranged immediately after the discharge point of the combustion devices, into which the combustion residues reach by the shortest route and in which they are optionally combusted by supplying further combustion air.
- FIG. 1 is a sectional view of a first embodiment of a boiler with a sloping grate as the primary combustion device and with a secondary burner,
- FIG. 2 shows a section through the fuel shaft with the primary combustion device and the secondary burner according to line A-A in FIG. 1,
- FIG. 3 shows a sectional illustration of a further embodiment of a heating boiler with a Sliding grate as primary combustion device and with a secondary burner,
- FIG. 4 shows a section through the fuel shaft with the primary combustion device and the secondary burner according to line A-A in FIG. 3,
- FIG. 5 shows a sectional illustration of an embodiment of a further steam generator with a feed grate for waste incineration as a primary combustion device and with a secondary burner,
- FIG. 6 shows a section through the primary combustion chamber with the primary combustion device and the secondary burner according to line A-A in FIG. 5,
- FIG. 7 shows a sectional illustration of an embodiment of a further steam generator with a rotary tube furnace as the primary combustion device and with a secondary burner
- Fig. 9 is a schematic sectional view of a
- a boiler comprises a voltage as Primär ⁇ combustion chamber serves fuel shaft 1 with a Ein Schollöff ⁇ 2, an inclined grate 3 as the primary combustion means, and an ash space 4.
- these ash chamber 4 to the primary ⁇ the solid fuel combustion necessary Primärverbren- air introduced.
- a fuel gas mixing chamber 6 is provided, into which the secondary combustion air required for the fuel gases for a complete gas burnout is supplied via a secondary grate 7 from a secondary air duct 8, via an inlet opening 9, the fuel gases enter a main combustion chamber 10, where they burn out completely. Thereafter, the optimally burned-out and hot gases leave the main combustion chamber 10 via an outlet opening 11 of the main combustion chamber 10 arranged offset to the inlet opening 9 and reach a waste heat area 12, where the thermal energy converted from the solid fuels can be used.
- the boiler shown in FIGS. 3 and 4 comprises a fuel shaft 1 with a bottom grate 13 and a revision opening 2.
- the primary combustion air necessary for primary combustion is introduced into space 4 below the bottom grate 13.
- the fuel gas mixing chamber 6 is provided, into which the secondary combustion air for the fuel gases for a complete gas burnout is supplied via the secondary grate 7 from the secondary air duct 8 the fuel gases enter the main combustion chamber 10, where they burn out completely.
- the optimal bronze burned and hot gases leave the main combustion chamber 10 via the offset relative to the inlet opening 9 arranged outlet opening 11 of the main combustion chamber 10 and pass into the Abhitze Scheme 12 where converted from the solid fuels Were eener- can be energy utilized.
- the steam generator according to FIGS. 5 and 6 comprises a primary ⁇ combustion chamber 12 with a ground-side feed grate 2 3 and a fuel feed device 22.
- the primary combustion air necessary for primary combustion is introduced under the feed grate 23.
- the fuel gas mixing chamber 6 is provided, into which the secondary combustion air for the fuel gases for a complete gas burnout is supplied from the secondary air duct 8 via the secondary grate 7.
- the combustion gases enter the main combustion chamber 10 via the inlet opening 9, where they burn out completely. Thereafter, the optimally burned-out and hot gases leave the main combustion chamber 10 via the outlet opening 11 of the main combustion chamber 10 which is offset from the inlet opening 9 and reach the waste heat region 12, where the heat energy converted from the solid fuels can be used.
- the steam generator shown in Figs. 7 and 8 comprises a primary combustion chamber 31 having a rotary kiln '33 with a fuel feed device 32 and a Schlacken ⁇ bay 35.
- the necessary for the primary combustion Verbren ⁇ is drying air ufgabeseite on the fuel 34 of the Dreh ⁇ kiln 33 in this initiated.
- the fuel gas mixing chamber 6 is provided, into which the secondary combustion air for the fuel gases for a complete gas burnout is supplied from the secondary air duct 8 via the secondary grate 7, via the inlet opening 9 the fuel gases enter the main combustion chamber 10, where they burn out completely. Thereafter, the optimally burned-out and hot gases leave the main combustion chamber 10 via the outlet opening 11 of the main combustion chamber 10 arranged offset to the inlet opening 9 and reach the waste heat area 12, where the heat energy converted from the solid fuels can be used.
- the volume of the main combustion chamber 10 is significantly larger than the volume of the Fire gas mixing chamber 6, and it is ensured, in particular by specifying the relative positions of the inflow and outflow openings, that a cyclone-shaped flow occurs in the main combustion chamber 10.
- the entire firing device can be modular. Both the fire gas mixing chamber 6 and the main combustion chamber 10 are provided with a corresponding refractory lining or lining, the height and width of the corresponding rooms being essentially the same, but the dimensions in the direction of flow of the gases are different.
- the Fig. 9 shows an immediately following a rotary kiln 33 and, accordingly, approximately below the Brandgasmischkam ⁇ mer 6 located internal shaft 16 with a Verbrennungs Kunststoff ⁇ supply 18 and a discharging device 19.
- the combustion residues 15 fall directly 'in these internal shaft 16.
- the combustion gases 17 come together with the combustion gases from the combustion device 33 into the combustion gas mixing chamber 6 and from there into the main combustion chamber 10, as indicated by arrows 17.
- the necessary combustion air for post-combustion of the residues is introduced into the combustion shaft 16 via the combustion air supply 18.
- the combustion residues 15 are discharged or removed from the combustion chamber 16 by the discharge device 19 after the complete burnout.
- the burner shaft 16 can isolated from the residues, but also cooled.
- a plurality of plate-shaped internals 14 arranged side by side with a catalytic effect, which make it possible to further minimize the CO content and even bring it to zero.
- These plate-shaped internals which, due to their arrangement, result in only a negligible flow resistance, take on high temperature during operation, in particular temperatures above 11000000 ° C. and then function primarily in the glowing state.
- the firing device for solid fuels according to the invention in the form of the burner system described for the combustion of solid fuels in the gaseous state in connection with known primary combustion devices provides a significantly better utilization of the available fuels compared to known firing devices while at the same time reducing the environmental impact from combustion-related pollutants and is also simple and economical to manufacture.
- the invented secondary combustion device in the form of the described combustion systems for burning solid fuels in gaseous state can be used in conjunction with all known primary devices.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Thermal Sciences (AREA)
- Incineration Of Waste (AREA)
- Combustion Of Fluid Fuel (AREA)
- Solid-Fuel Combustion (AREA)
Abstract
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19883809429 DE3809429A1 (de) | 1988-03-21 | 1988-03-21 | Brennersystem zur verbrennung von festen brennstoffen in gasfoermigem zustand |
DE3809429 | 1988-03-21 |
Publications (1)
Publication Number | Publication Date |
---|---|
EP0362348A1 true EP0362348A1 (fr) | 1990-04-11 |
Family
ID=6350275
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19890904036 Withdrawn EP0362348A1 (fr) | 1988-03-21 | 1989-03-21 | Appareil de combustion pour bruler des combustibles solides |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0362348A1 (fr) |
JP (1) | JPH02504668A (fr) |
DE (1) | DE3809429A1 (fr) |
WO (1) | WO1989009364A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7329711B2 (en) | 2001-11-12 | 2008-02-12 | Basf Aktiengesellschaft | Modified epoxy resins |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4033406A1 (de) * | 1990-10-20 | 1992-04-23 | Hoval Interliz Ag | Verfahren und vorrichtung zum verfeuern von holzschnitzeln und holzspaenen unter bildung schadstoffarmer abgase bei gleitend regelbarer feuerungsleistung |
GB9121648D0 (en) * | 1991-10-11 | 1991-11-27 | D & C Eng Bv | A combustor apparatus |
JP6621028B2 (ja) * | 2016-09-14 | 2019-12-18 | 株式会社ソラール | 籾殻燃焼温水ボイラー及び燃焼方法 |
Family Cites Families (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR56447E (fr) * | 1941-10-23 | 1952-09-24 | Cie Des Procedes Gohin Poulenc | Dispositif de chauffage par gazogène et son application aux fours à températures élevées |
FR1412396A (fr) * | 1964-02-13 | 1965-10-01 | Procédé et dispositif de post-combustion pour foyers à combustible solide | |
US4334484A (en) * | 1980-01-18 | 1982-06-15 | University Of Kentucky Research Foundation | Biomass gasifier combustor |
EP0050105A3 (fr) * | 1980-10-09 | 1982-09-29 | Kurt Sjöstrand | Procédé et dispositif pour la combustion de combustibles solides |
IT1158514B (it) * | 1982-01-13 | 1987-02-18 | Tecnitalia Spa | Impianto di incenerimento di rifiuti con forno in equicorrente |
US4483256A (en) * | 1982-02-24 | 1984-11-20 | Clayton & Lambert Manufacturing Co. | Biomass gasifier combustor system and components therefor |
WO1985001096A1 (fr) * | 1983-08-31 | 1985-03-14 | Egon Krogemann | Installation de combustion de combustibles biologiques |
NZ210243A (en) * | 1984-11-19 | 1988-01-08 | Waterwide Dev New Zealand Ltd | Extraction zone for solid fuel burner |
US4691846A (en) * | 1985-06-11 | 1987-09-08 | Cordell Henry L | Method and apparatus for gasifying solid organic materials |
DE3715648A1 (de) * | 1987-05-11 | 1988-11-24 | Thermo Anlagen Technik Miehe G | Verfahren und einrichtung zur thermischen verwertung von brikettierten brennbaren fest-stoffen, vornehmlich solchen aus abfaellen, bestehend aus mindestens drei in reihe geschalteten teilanlagen wie brennraeumen und gasreinigungen |
-
1988
- 1988-03-21 DE DE19883809429 patent/DE3809429A1/de not_active Withdrawn
-
1989
- 1989-03-21 EP EP19890904036 patent/EP0362348A1/fr not_active Withdrawn
- 1989-03-21 WO PCT/EP1989/000303 patent/WO1989009364A1/fr not_active Application Discontinuation
- 1989-03-21 JP JP50371989A patent/JPH02504668A/ja active Pending
Non-Patent Citations (1)
Title |
---|
See references of WO8909364A1 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7329711B2 (en) | 2001-11-12 | 2008-02-12 | Basf Aktiengesellschaft | Modified epoxy resins |
Also Published As
Publication number | Publication date |
---|---|
DE3809429A1 (de) | 1989-10-12 |
WO1989009364A1 (fr) | 1989-10-05 |
JPH02504668A (ja) | 1990-12-27 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE FR GB IT LI LU NL SE |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: HARLANDER, NORBERT |
|
DIN1 | Information on inventor provided before grant (deleted) | ||
17P | Request for examination filed |
Effective date: 19891220 |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: HARLANDER, NORBERT |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: HARLANDER, JOSEF |
|
17Q | First examination report despatched |
Effective date: 19910517 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
18D | Application deemed to be withdrawn |
Effective date: 19911127 |