EP0084279A2 - Verfahren und Einrichtung zur Wärmerückgewinnung, insbesondere bei der Abkühlung von Asche - Google Patents
Verfahren und Einrichtung zur Wärmerückgewinnung, insbesondere bei der Abkühlung von Asche Download PDFInfo
- Publication number
- EP0084279A2 EP0084279A2 EP82402145A EP82402145A EP0084279A2 EP 0084279 A2 EP0084279 A2 EP 0084279A2 EP 82402145 A EP82402145 A EP 82402145A EP 82402145 A EP82402145 A EP 82402145A EP 0084279 A2 EP0084279 A2 EP 0084279A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- ash
- ashes
- finest
- fluidized bed
- fumes
- 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
- 239000002956 ash Substances 0.000 title claims abstract description 54
- 235000002918 Fraxinus excelsior Nutrition 0.000 title claims abstract description 26
- 238000009434 installation Methods 0.000 title claims abstract description 9
- 238000000034 method Methods 0.000 title claims abstract description 8
- 238000001816 cooling Methods 0.000 title claims description 15
- 239000002245 particle Substances 0.000 claims abstract description 16
- 239000003517 fume Substances 0.000 claims abstract description 14
- 238000010926 purge Methods 0.000 claims abstract description 8
- 238000002485 combustion reaction Methods 0.000 claims abstract description 5
- 239000007787 solid Substances 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 12
- 239000000446 fuel Substances 0.000 claims description 7
- 238000011084 recovery Methods 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 239000000779 smoke Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- 239000003546 flue gas Substances 0.000 claims 1
- 235000015076 Shorea robusta Nutrition 0.000 description 2
- 244000166071 Shorea robusta Species 0.000 description 2
- 241001180699 Phengaris arion Species 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
Definitions
- the subject of the invention is a method and an installation for recovering the heat contained in a solid body in divided form, and applies more particularly to the cooling of the ashes of poor fuels.
- the body is separated into several parts of particle size corresponding for each to a determined range and each part is passed through a cooling device specially adapted to its particle size.
- This process finds a particularly advantageous application in the case of poor fuels which are generally burned in a fluidized bed because this allows stable combustion and is satisfied with coarse grinding, for example between 0 and 10 mm.
- the fluidized bed has the particularity of carrying out itself, during combustion, a separation of the ash produced according to their particle size.
- the finest ashes for example less than 0.5 mm, are entrained by the ascending gaseous current discharged with the fumes while the ashes of larger particle size, for example between 0.5 and 10 mm remain in the fluidized bed.
- advantage is taken of this separation carried out by said fluidized itself to adapt the cooling mode to the particle size. ash and use coolers at their optimum performance.
- the large blues are removed from the ashes by the purge outlet from the fluidized bed, the finest ashes are separated from the fumes escaping from the oven and the two parts of the ashes thus collected are cooled in two cooling each adapted to the particle size, one of the finest ashes and the other of the largest ashes.
- the coarsest ashes are cooled by circulation of air against the current and the finest ashes in a fluidized bed and the air heated by the coarsest ashes is mixed with the smoke leaving the oven after separation of the fine ash, said smoke and the air heated by the fine ash being then introduced at two different points in a circuit for using the heat of the gases thus heated.
- the installation for implementing the method according to the invention therefore comprises two cooling devices fed one by the largest ash removed by the purge outlet and the other by the finest ash removed by a separator on the fumes coming out of the oven.
- the appended figure schematically shows, by way of example, such an installation.
- This comprises a fluidized bed oven consisting of an enclosure 1 provided at its lower part with a grid 11 limiting a chamber 12 for the arrival of fluidization gas.
- the fuel supplied by an inlet 13 burns in the fluidized bed formed above the grid 11 and the fumes are evacuated through the chimney 14.
- An outlet 15 placed at the height of the fluidized bed and produced in a conventional manner makes it possible to carry out a purge by evacuating the largest ashes while the finest ashes escape with the fumes through the chimney 14.
- the ash leaving through the drain 15 feeds a cooler 2 constituted for example by an inclined rotary drum inside which the ashes descend, against the flow of the cooling gas such as air which is introduced cold at 21, circulates solid matter in the opposite direction and exits at 22 at a temperature of the order of 800 ° C.
- a cooler 2 constituted for example by an inclined rotary drum inside which the ashes descend, against the flow of the cooling gas such as air which is introduced cold at 21, circulates solid matter in the opposite direction and exits at 22 at a temperature of the order of 800 ° C.
- the fumes which escape through the chimney 14 at a temperature of approximately 900 ° C. first pass through a static separator 3, for example a cyclone and are directed by a pipe 31 for discharging the gases towards a circuit d use, for example a recovery boiler 4.
- the finest ash entrained in the chimney 14 by the fumes is therefore collected at the bottom of the separator 3, at a temperature of about 900 ° C and supply a cooler adapted to their particle size, for example a fluidized bed 5.
- This is supplied by cold air which is distributed under the grid, passes through it with a low speed and leaves in 51 at a temperature of around 500 °.
- the air at 800 ° leaving at 22 from the counter-current cooler 2 is evacuated through a line 23 which opens into the line 31 upstream of the boiler 4 which is thus supplied with the mixture which circulates inside the boiler by cooling for example on water circulation beams for the production of steam.
- the air at 500 ° leaving at 51 from the cooler 5 can therefore be introduced further downstream in the recovery boiler, in an area where the fumes have already been cooled to a temperature of about 500 °.
- each of the two coolers operates for the particle size to which it is adapted and the hot gases produced are used under optimal conditions.
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT82402145T ATE19688T1 (de) | 1981-11-27 | 1982-11-25 | Verfahren und einrichtung zur waermerueckgewinnung, insbesondere bei der abkuehlung von asche. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8122228A FR2517419A1 (fr) | 1981-11-27 | 1981-11-27 | Procede et installation de recuperation de chaleur, notamment pour le refroidissement de cendres |
FR8122228 | 1981-11-27 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0084279A2 true EP0084279A2 (de) | 1983-07-27 |
EP0084279A3 EP0084279A3 (en) | 1983-08-10 |
EP0084279B1 EP0084279B1 (de) | 1986-05-07 |
Family
ID=9264427
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP82402145A Expired EP0084279B1 (de) | 1981-11-27 | 1982-11-25 | Verfahren und Einrichtung zur Wärmerückgewinnung, insbesondere bei der Abkühlung von Asche |
Country Status (7)
Country | Link |
---|---|
US (1) | US4471723A (de) |
EP (1) | EP0084279B1 (de) |
JP (1) | JPS58173312A (de) |
AT (1) | ATE19688T1 (de) |
BR (1) | BR8206856A (de) |
DE (1) | DE3271053D1 (de) |
FR (1) | FR2517419A1 (de) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108980820A (zh) * | 2018-07-16 | 2018-12-11 | 重庆大学 | 一种循环流化床锅炉底渣余热回收装置 |
CN110052223A (zh) * | 2019-05-20 | 2019-07-26 | 陕西金泰氯碱化工有限公司 | 一种无汞催化合成氯乙烯采用高沸点水溶液移热的装置 |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2723402A (en) * | 1950-07-12 | 1955-11-15 | Lloyd V France | Propolis culture |
JPS61175408A (ja) * | 1985-01-31 | 1986-08-07 | Chiyuushiyou Kigyo Shinko Jigyodan | 石炭ボイラ燃焼灰の冷却方法 |
DE3625992A1 (de) * | 1986-07-31 | 1988-02-04 | Steinmueller Gmbh L & C | Verfahren zum verbrennen von kohlenstoffhaltigen materialien in einer zirkulierenden wirbelschicht und wirbelschichtfeuerungsanlage zur durchfuehrung des verfahrens |
SE459987B (sv) * | 1987-12-23 | 1989-08-28 | Abb Stal Ab | Saett att kyla aska och kraftanlaeggning med en anordning foer askkylning |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB317470A (en) * | 1928-08-18 | 1931-01-02 | Geza Szikla | Improvements in or relating to coal dust furnaces |
FR1221397A (fr) * | 1958-03-24 | 1960-06-01 | Cie Metaux Doverpelt Lommel | Procédé pour la valorisation de combustibles très cendreux et à pouvoir calorifique très faible |
DE1166402B (de) * | 1958-11-04 | 1964-03-26 | Cie Des Metaux D Overpelt Lomm | Wirbelbettfeuerung zur Verbrennung geringwertiger Brennstoffe in zwei Verbrennungskammern |
GB1032598A (en) * | 1963-10-14 | 1966-06-15 | Fuji Photo Film Co Ltd | Improvements in or relating to heating apparatus |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2624302C2 (de) * | 1976-05-31 | 1987-04-23 | Metallgesellschaft Ag, 6000 Frankfurt | Verfahren zur Durchführung exothermer Prozesse |
US4159682A (en) * | 1977-12-01 | 1979-07-03 | Dorr-Oliver Incorporated | Fluid bed combustion with predrying of moist feed using bed sand |
US4196676A (en) * | 1978-07-21 | 1980-04-08 | Combustion Power Company, Inc. | Fluid bed combustion method and apparatus |
US4349969A (en) * | 1981-09-11 | 1982-09-21 | Foster Wheeler Energy Corporation | Fluidized bed reactor utilizing zonal fluidization and anti-mounding pipes |
US4355601A (en) * | 1981-09-25 | 1982-10-26 | Conoco Inc. | Recirculating flue gas fluidized bed heater |
-
1981
- 1981-11-27 FR FR8122228A patent/FR2517419A1/fr active Granted
-
1982
- 1982-11-22 US US06/443,817 patent/US4471723A/en not_active Expired - Fee Related
- 1982-11-25 EP EP82402145A patent/EP0084279B1/de not_active Expired
- 1982-11-25 AT AT82402145T patent/ATE19688T1/de active
- 1982-11-25 DE DE8282402145T patent/DE3271053D1/de not_active Expired
- 1982-11-26 BR BR8206856A patent/BR8206856A/pt unknown
- 1982-11-27 JP JP57208385A patent/JPS58173312A/ja active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB317470A (en) * | 1928-08-18 | 1931-01-02 | Geza Szikla | Improvements in or relating to coal dust furnaces |
FR1221397A (fr) * | 1958-03-24 | 1960-06-01 | Cie Metaux Doverpelt Lommel | Procédé pour la valorisation de combustibles très cendreux et à pouvoir calorifique très faible |
DE1166402B (de) * | 1958-11-04 | 1964-03-26 | Cie Des Metaux D Overpelt Lomm | Wirbelbettfeuerung zur Verbrennung geringwertiger Brennstoffe in zwei Verbrennungskammern |
GB1032598A (en) * | 1963-10-14 | 1966-06-15 | Fuji Photo Film Co Ltd | Improvements in or relating to heating apparatus |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108980820A (zh) * | 2018-07-16 | 2018-12-11 | 重庆大学 | 一种循环流化床锅炉底渣余热回收装置 |
CN110052223A (zh) * | 2019-05-20 | 2019-07-26 | 陕西金泰氯碱化工有限公司 | 一种无汞催化合成氯乙烯采用高沸点水溶液移热的装置 |
Also Published As
Publication number | Publication date |
---|---|
EP0084279A3 (en) | 1983-08-10 |
JPS58173312A (ja) | 1983-10-12 |
BR8206856A (pt) | 1983-10-04 |
FR2517419A1 (fr) | 1983-06-03 |
DE3271053D1 (en) | 1986-06-12 |
FR2517419B3 (de) | 1984-08-24 |
ATE19688T1 (de) | 1986-05-15 |
US4471723A (en) | 1984-09-18 |
EP0084279B1 (de) | 1986-05-07 |
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BE541056A (de) |
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