EP0063629A1 - Alimentation en charbon pulvérisé - Google Patents
Alimentation en charbon pulvérisé Download PDFInfo
- Publication number
- EP0063629A1 EP0063629A1 EP81103220A EP81103220A EP0063629A1 EP 0063629 A1 EP0063629 A1 EP 0063629A1 EP 81103220 A EP81103220 A EP 81103220A EP 81103220 A EP81103220 A EP 81103220A EP 0063629 A1 EP0063629 A1 EP 0063629A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- coal dust
- burner
- fluidized bed
- reactor
- line
- 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
Links
- 239000002817 coal dust Substances 0.000 title claims abstract description 26
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 6
- 239000001301 oxygen Substances 0.000 claims abstract description 6
- 239000002245 particle Substances 0.000 claims description 18
- 239000000567 combustion gas Substances 0.000 claims description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 1
- 239000003921 oil Substances 0.000 claims 1
- 239000000523 sample Substances 0.000 claims 1
- 238000010792 warming Methods 0.000 claims 1
- 239000012530 fluid Substances 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 1
- 239000003546 flue gas Substances 0.000 abstract 1
- 239000000428 dust Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000007654 immersion Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 241000273930 Brevoortia tyrannus Species 0.000 description 1
- 241000251730 Chondrichthyes Species 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
Definitions
- the invention relates to an entry of coal dust into a burner or Raaktor.
- Coal dust input is a problem area in coal dust burners and in throat dust reactors.
- the uniformity of the coal dust supply is decisive for the quality of a throat dust inlet
- Zutsil devices such as cellular wheel locks, screw conveyor scales, etc. only loosen up the dust particle mix in bunkers and imperfectly, so that the material of different bulk densities clumps together in larger units and enters the burner. This leads to a fluctuating material flow, which is extremely unfavorable for combustion. At gl3ich. permanent oxygen supply then comes to unsuspicious reactions and to a decrease in the burner or Reactor power. Usually the pulsing of the Srennars or reactor is gas-spoken.
- the object of the invention is to create a cooling entry system for coal dust greeners and reactors, which ensures a uniform entry flow of coal dust particles.
- Oabsi emanates from the invention the idea of entering the coal particles intended for combustion as far as possible into the race or reactor with gas rings spaced from one another, so that each coal dust particle always receives the optimum oxygen content for combustion.
- this is achieved by a fluidized bed with at least one immersed tube which projects into the fluidized bed and leads to the burner or reactor as a metering device or an air / oxygen or vitrified solution solution to the burner or reactor as a metering device, the line closing an intermittently Has opening.
- the coal dust particles are fluidized in the fluidized bed. 3the particle is enveloped with air by itself and, when it is reached, is introduced from the fluidized bed into the burner or reactor.
- Both the immersion tube and the line leading through the swirl bed according to the invention, as a metering device, enable an absolutely uniform entry which is infinitely variable in its quantity.
- Oxygen can also be coated with oil or other combustion gas in the fluidized bed, since the fluidized bed is also an extremely suitable mixing device. Depending on the low temperature, liquid oxygen can also be mixed with the coal dust particles. In another way, the vortex bed also preheats the coal dust particle by partially burning and / or supplying suitable shark gases.
- the coal dust particles intended for a burner are fluidized into a container 1 by means of blown-in air.
- the coal dust particles are continuously conveyed into the container 1 from above via a schematically illustrated, adjustable cell lock 2.
- the air enters the container 1 through an air supply line 3 below and swirls the coal dust particles in the container 1.
- a fuel line 4 leads through the container 1.
- the burner line leads from the container 1 to the dsm burner, not shown.
- the Brsnnsr effet 4 has a recess within the container, which is filled by a rotatably arranged perforated disk 5. Instead of the perforated disc, a rotating cylinder Ver. find application.
- the decisive factor is that there are through holes in the rotating body into which the carbon dust particles swirled in the container 1 can penetrate. Da3 requires a sufficient dwell time of the through-hole outside of the Brsnnorleeitung 4.
- the Vorwsil from the speed of the Lochsehsibs 5 and its diameter, which is a multiple of the fürmossors the
- the carbon dust particles that have penetrated are carried into the burner line 4 and discharged there to the burner by means of combustion air fed into the burner line 4.
- the flow rate of the entry device according to the invention according to FIG. 1 can also be changed continuously by changing the speed of the rotating perforated disk.
- an immersion tube 6 is arranged in the container 1 so that it can be advanced.
- the dip tube 6 penetrates into the container 1 from above and is adjustable in height. It leads from the container 1 to the Brennsr, not shown. This allows the air pressed into the container 1 to escape through the dip tube 6 to the burner. This air takes the swirled coal dust particles in the container 1 and carries them into the burner.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP81103220A EP0063629B1 (fr) | 1981-04-29 | 1981-04-29 | Alimentation en charbon pulvérisé |
AT81103220T ATE22605T1 (de) | 1981-04-29 | 1981-04-29 | Kohlenstaubeintrag. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP81103220A EP0063629B1 (fr) | 1981-04-29 | 1981-04-29 | Alimentation en charbon pulvérisé |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP83111807.0 Division-Into | 1981-04-29 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0063629A1 true EP0063629A1 (fr) | 1982-11-03 |
EP0063629B1 EP0063629B1 (fr) | 1986-10-01 |
Family
ID=8187683
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP81103220A Expired EP0063629B1 (fr) | 1981-04-29 | 1981-04-29 | Alimentation en charbon pulvérisé |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0063629B1 (fr) |
AT (1) | ATE22605T1 (fr) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0066984B1 (fr) * | 1981-06-09 | 1984-07-25 | Coal Industry (Patents) Limited | Système pour la distribution de matériau pulvérulent |
EP0130316A1 (fr) * | 1983-05-13 | 1985-01-09 | Ruhrkohle-Carborat GmbH | Dispositif d'alimentation pneumatique à charbon pulvérisé |
EP0247235A1 (fr) * | 1986-05-23 | 1987-12-02 | Ruhrkohle-Carborat GmbH | Dispositif de transport d'air comprimé et dispositif doseur |
WO2009095290A2 (fr) * | 2008-01-31 | 2009-08-06 | Siemens Aktiengesellschaft | Système de dosage de poussières |
DE102008014475A1 (de) * | 2008-03-17 | 2009-11-12 | Uhde Gmbh | Verfahren und Vorrichtung zur dosierten Entnahme eines fein- bis grobkörnigen Feststoffes oder Feststoffgemisches aus einem Vorratsbehälter |
CN111964041A (zh) * | 2020-08-26 | 2020-11-20 | 界首市华盛塑料机械有限公司 | 一种供能机构及基于该机构的锅炉辅机 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT92107B (de) * | 1918-11-26 | 1923-04-10 | Comb E Economica Societa Anoni | Brennstaubfeuerung. |
DE393345C (de) * | 1921-05-27 | 1924-04-08 | Arbed | Vorrichtung zum Mischen von Brennstoff und Primaerluft bei Kohlenstaubfeuerungen |
DE456237C (de) * | 1924-03-11 | 1928-02-22 | Int Comb Eng Corp | Verfahren zur Herstellung eines Brennstaubluftgemisches von Einfuehrung desselben in eine Feuerkammer |
DE2654662A1 (de) * | 1975-12-04 | 1977-06-08 | Shell Int Research | Verfahren und vorrichtung zur teilverbrennung von kohlestaub |
-
1981
- 1981-04-29 EP EP81103220A patent/EP0063629B1/fr not_active Expired
- 1981-04-29 AT AT81103220T patent/ATE22605T1/de not_active IP Right Cessation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT92107B (de) * | 1918-11-26 | 1923-04-10 | Comb E Economica Societa Anoni | Brennstaubfeuerung. |
DE393345C (de) * | 1921-05-27 | 1924-04-08 | Arbed | Vorrichtung zum Mischen von Brennstoff und Primaerluft bei Kohlenstaubfeuerungen |
DE456237C (de) * | 1924-03-11 | 1928-02-22 | Int Comb Eng Corp | Verfahren zur Herstellung eines Brennstaubluftgemisches von Einfuehrung desselben in eine Feuerkammer |
DE2654662A1 (de) * | 1975-12-04 | 1977-06-08 | Shell Int Research | Verfahren und vorrichtung zur teilverbrennung von kohlestaub |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0066984B1 (fr) * | 1981-06-09 | 1984-07-25 | Coal Industry (Patents) Limited | Système pour la distribution de matériau pulvérulent |
EP0130316A1 (fr) * | 1983-05-13 | 1985-01-09 | Ruhrkohle-Carborat GmbH | Dispositif d'alimentation pneumatique à charbon pulvérisé |
EP0247235A1 (fr) * | 1986-05-23 | 1987-12-02 | Ruhrkohle-Carborat GmbH | Dispositif de transport d'air comprimé et dispositif doseur |
WO2009095290A2 (fr) * | 2008-01-31 | 2009-08-06 | Siemens Aktiengesellschaft | Système de dosage de poussières |
WO2009095290A3 (fr) * | 2008-01-31 | 2011-03-10 | Siemens Aktiengesellschaft | Système de dosage de poussières |
DE102008014475A1 (de) * | 2008-03-17 | 2009-11-12 | Uhde Gmbh | Verfahren und Vorrichtung zur dosierten Entnahme eines fein- bis grobkörnigen Feststoffes oder Feststoffgemisches aus einem Vorratsbehälter |
CN111964041A (zh) * | 2020-08-26 | 2020-11-20 | 界首市华盛塑料机械有限公司 | 一种供能机构及基于该机构的锅炉辅机 |
Also Published As
Publication number | Publication date |
---|---|
EP0063629B1 (fr) | 1986-10-01 |
ATE22605T1 (de) | 1986-10-15 |
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