FI70528C - Apparatus for separating solids in circulating bed reactor. - Google Patents
Apparatus for separating solids in circulating bed reactor. Download PDFInfo
- Publication number
- FI70528C FI70528C FI844442A FI844442A FI70528C FI 70528 C FI70528 C FI 70528C FI 844442 A FI844442 A FI 844442A FI 844442 A FI844442 A FI 844442A FI 70528 C FI70528 C FI 70528C
- Authority
- FI
- Finland
- Prior art keywords
- reactor
- solids
- vortex chamber
- vortex
- bed reactor
- Prior art date
Links
- 239000007787 solid Substances 0.000 title claims description 21
- 239000007789 gas Substances 0.000 claims description 20
- 238000000926 separation method Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000007872 degassing Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
-
- 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
- B01J8/005—Separating solid material from the gas/liquid stream
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/04—Multiple arrangement thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2900/00—Special arrangements for conducting or purifying combustion fumes; Treatment of fumes or ashes
- F23J2900/15026—Cyclone separators with horizontal axis
Description
Laite kiintoaineen erottamiseksi kiertopetireaktorissaApparatus for separating solids in a circulating bed reactor
Anordning för avskiljning av fast material i reaktor med cirkulerande bädd 1 70528Anordning avskiljning av fast material i Reaktor med circulerande bädd 1 70528
Esillä oleva keksintö kohdistuu kiertopetireaktorin yhteydessä käytettävään laitteeseen kiintoaineen erottamiseksi reaktorin poistokaasuista ja kiintoaineen palauttamiseksi reaktor iin.The present invention relates to an apparatus for use in connection with a circulating bed reactor for separating solids from reactor exhaust gases and returning solids to the reactor.
Keksinnön tarkoituksena on saada aikaan laite, jolla kierto-peti reaktorin poistokaasuista voidaan tehokkaasti erottaa kiintoainetta ja palauttaa haluttuun kohtaan reaktoriin.The object of the invention is to provide a device with which a solid can be efficiently separated from the exhaust gases of a circulating bed reactor and returned to the desired location in the reactor.
Kiertopetitekniikkaa on sovellettu kauan mm. pasutoissa ja nykyisin enenevässä määrin erilaisissa reaktoreissa, kuten poIttopesissä ja kaasuttimissa. Tunnetuissa sovellutuksissa kiintoaineen erottaminen kaasuista tapahtuu tavanomaisessa, alaosaltaan suppiIonmuotoisessa sykI onierottimessa, jossa olevaan syIinterimäiseen pyörrekammioon on sovitettu kaasuja ylöspäin johtava kaasunpoistoputki ja josta kiintoaine palautetaan reaktoriin kaasulukon kautta. Kaasulukon tehtävänä on estää reaktorikaasujen virtaus sykloniin laskuputken kautta. Yleisimmin tällaisena kaasulukkona toimii mekaaninen sulkulaite tai kehittyneemmissä laitteissa U-putkessa leijuva hiekka. Varsinkin korkea Iämpöti Iareaktoreissa tulee kiintomateriaa I in palautusjärjestelmästä monimutkainen ja kallis. Osa kaasulukon leijutukseen tarvittavasta ilmasta virtaa Iaskuputkessa ylöspäin ja tällä on haitallinen vaikutus erityisesti kevyen ja hienojakeisen materiaalin erottumiseen. Lisäksi nouseva kaasuvirtaus pienentää lasku-putken kuljetuskapasiteettia.The rotary bed technology has been applied for a long time e.g. roasters and, increasingly, in various reactors such as combustors and carburettors. In known applications, the separation of solids from gases takes place in a conventional, constricted, bottom-shaped cycle separator, in which a cylindrical vortex chamber is fitted with a gas-carrying exhaust pipe and from which the solids are returned to the reactor via a gas trap. The purpose of the gas trap is to prevent the flow of reactor gases into the cyclone through the downcomer. The most common such gas lock is a mechanical shut-off device or, in more advanced devices, sand floating in a U-tube. Especially high temperature reactors become the solids I in the recovery system complex and expensive. Some of the air required to fluidize the gas trap flows upwards in the exhaust pipe and this has a detrimental effect, especially on the separation of light and fine material. In addition, the ascending gas flow reduces the conveying capacity of the downcomer.
Tavanomaisessa syklonissa muodostuu tunnetusti keskelle voimakas alipaine ja suuri aksiaalinen virtausnopeus. Tästä johtuen tavanomainen sykloni pyrkii imemään Iaskuputkesta. Syntyvällä imuvirtaukseII a ei yleensä ole tangentiaa I i nopeutta, joten lähes kaikki sen mukanaan kuljettama kiinto- 2 70528 aine kulkeutuu syklonin keskusputken kautta ulos. Tavanomaisella syklonilla varustettu palautusjärjestelmä on siis erittäin herkkä paluuputken imuvirtauksiI Ie ja vaatii luotettavan kaasulukon.In a conventional cyclone, a strong vacuum and a high axial flow rate are known to form in the middle. Because of this, a conventional cyclone tends to suck from the inlet tube. The resulting suction flow generally does not have a tangential velocity, so that almost all of the solids it carries pass through the cyclone center tube. Thus, a return system equipped with a conventional cyclone is very sensitive to the suction flows of the return pipe and requires a reliable gas trap.
HöyrykattiIasoveI Iutuksissa tavanomaisen syklonin käyttö johtaa epäedulliseen rakenteeseen, koska tavanomainen sykloni jakaa kattilan erilliseen polttopesään ja syklonin jälkeiseen konvektio-osaan, joiden välissä sijaitsevat ki intomateriaalin palautuslaitteet.In steam boiler applications, the use of a conventional cyclone results in an unfavorable structure because the conventional cyclone divides the boiler into a separate combustion chamber and a post-cyclone convection section, between which are located the material recovery devices.
Mekaaniset kaasulukot kuluvat nopeasti erityisesti kuumissa olosuhteissa ja niissä esiintyy usein käyttöhäiriöitä.Mechanical gas locks wear rapidly, especially in hot conditions, and often malfunction.
Tunnettuja ovat myöskin ratkaisut, joissa reaktorin sisään asennetaan tavanomainen sykloni, jolloin koko kiintoaineen palautusjärjestelmä sijaitsee reaktorin sisällä. Tässä järjestelmässä esiintyy suurina haittoina syklonin korroosio-ja eroosio-ongelmia, koska tukirakenteen jäähdytystä ei yksinkertaisin keinoin voida järjestää. Lisäksi systeemi kärsii tavanomaisen syklonin herkkyydestä paluuputken imu-v i rtauks i I I e.Solutions are also known in which a conventional cyclone is installed inside the reactor, in which case the entire solids recovery system is located inside the reactor. Cyclone corrosion and erosion problems are major drawbacks in this system because cooling of the support structure cannot be provided by simple means. In addition, the system suffers from the sensitivity of a conventional cyclone to the return suction of the return pipe.
Keksinnön tarkoituksena on aikaansaada laite, jolla edellä mainituissa laitteissa esiintyvät epäkohdat voidaan poistaa ja jolla voidaan saavuttaa korkea erotusaste. Tämän päämäärän saavuttamiseksi käyteään 2-vaihe- tai monivaihe-erotus-ta, jossa ensimmäisessä vaiheessa poistetaan karkeita kuluttavia partikkeleita pienimmillä kehänopeuksiI I a ja seuraavissa vaiheissa pienempiä hiukkasia suurilta kehänopeuks i I I a.The object of the invention is to provide a device with which the drawbacks present in the above-mentioned devices can be eliminated and with which a high degree of separation can be achieved. To achieve this goal, a 2-stage or multi-stage separation is used, in which the first step removes coarse abrasive particles at the lowest circumferential speeds Ia and in the subsequent steps smaller particles at high circumferential speeds Iaa.
Keksinnön mukaiselle laitteelle on tunnusomaista se, että se käsittää kaksi erikokoista, pääasiallisesti vaakasuoraa, vierekkäistä, samankeskistä pyörrekammi ota, joissa on pyörrekammioiden kanssa samankeskiset kaasunpoistoaukot ja joista halkaisijaltaan pienempi on varustettu pyörrekammion 3 70528 kanssa samankeskisellä, halkaisijaltaan suuremman pyörre-kammion kaasunpoistoaukkoon yhdistetyllä kaasuntuIoaukoI I a.The device according to the invention is characterized in that it comprises two differently sized, substantially horizontal, adjacent, concentric vortex chambers with concentric degassing openings with the vortex chambers, the smaller diameter of which is provided with a vortex chamber 370528 .
Keksintöä selostetaan seuraavassa lähemmin viitaten oheisiin piirustuksiin, joissa kuvio 1 esittää erästä keksinnön suoritusmuotoa pystyleik-kauksena, ja kuvio 2 esittää kuvion 1 leikkausta viivaa B - B pitkin.The invention will now be described in more detail with reference to the accompanying drawings, in which Figure 1 shows an embodiment of the invention in vertical section, and Figure 2 shows a section of Figure 1 along the line B-B.
Kuvioissa viitenumero 1 tarkoittaa pystysuoraa kierto-peti reaktoria, jonka yläosasta poistuvat kaasut johdetaan kahdella vaakasuoralla pyörrekammio I I a varustetun erotus-laitteen 4 ensimmäiseen pyörrekammioon 2 siihen tangentiaa-lisesti liittyvän kaasuntuIokanavan 3 kautta. Pyörrekammion kehälle erottunut kiintoaine poistuu siinä olevan aukon 5 kautta pyörrekammiosta ja virtaa pyörrekammioon tangentiaa-lisesti liittyvän pa I autuskanavan 6 kautta takaisin reaktoriin. Toinen, halkaisijaltaan pienempi pyörrekammio 10 on liitetty ensimmäisen pyörrekammion toisessa päädyssä 7 olevaan kaasunpoistoaukkoon 8. Pyörrekammion kehälle erottunut kiintoaine poistuu siinä olevan aukon kautta pyörre-kammiosta ja palautetaan pa Iautuskanavan 11 kautta reaktoriin tai poistetaan järjestelmästä poistokanavan 12 kautta.In the figures, reference numeral 1 denotes a vertical rotary bed reactor, the gases leaving the upper part of which are led to the first vortex chamber 2 of a separating device 4 provided with two horizontal vortex chambers Iaa through a gas trough tangentially connected thereto. The solid separated on the circumference of the vortex chamber exits the vortex chamber through the opening 5 therein and flows back to the reactor through the passage channel 6 tangentially connected to the vortex chamber. A second, smaller diameter vortex chamber 10 is connected to a degassing opening 8 at the second end 7 of the first vortex chamber. The solid separated on the circumference of the vortex chamber exits the vortex chamber through an opening therein and is returned to the reactor via a discharge duct 11 or discharged from the system.
Puhdistetut kaasut virtaavat pyörrekammion 10 päädyssä 13 olevan aukon 14 kautta konvektio-osaan 9.The purified gases flow through the opening 14 in the end 13 of the vortex chamber 10 to the convection section 9.
Virtausteknisesti keksinnön mukainen järjestelmä eroaa tavanomaisesta mm. siten, että kiintoaine palautuu reaktoriin kaasuvirtauksen (1 - 10 % kaasuista) kuljettamana.In terms of flow technology, the system according to the invention differs from the conventional e.g. so that the solid returns to the reactor by a gas flow (1-10% of the gases).
Koska kiintoaineen poistumiskohta on pyörrekammion kehällä, missä kiintoaineen nopeus on suurimmillaan, saavutetaan hyvä erotuskyky.Since the solids exit point is on the circumference of the vortex chamber, where the solids velocity is at its highest, good resolution is achieved.
11 7052811 70528
Keksinnön mukaisella järjestelmällä saadaan ilmeisiä rakenteellisia etuja, joista mainittakoon: - kompakti rakenne - paisuntasaumoja voidaan välttää - kiertopetireaktori voidaan paineistaa aiheuttamatta huomattavia lisäkustannuksia.The system according to the invention provides obvious structural advantages, such as: - compact structure - expansion joints can be avoided - the circulating bed reactor can be pressurized without causing significant additional costs.
Kiintoaine voidaan poistaa pyörrekammiosta yhden yli koko pyörrekammion leveyden ulottuvan aukon ja siihen liitetyn pa Iautuskanavan kautta tai useiden vierekkäisten aukkojen ja pa Iautuskanavien kautta.The solids can be removed from the vortex chamber through an opening extending over the entire width of the vortex chamber and the associated passage channel, or through a plurality of adjacent openings and passage channels.
Pa Iautuskanavat voidaan varustaa jäähdytysvaipa I I a, mikäli reaktoriin palautettava kiintoaine halutaan jäähdyttää. Pa I autuskanavat voidaan varustaa venttiilillä niin, että osa kanavista voidaan sulkea. Pa Iautuskanavien Iiittyrniskohdat voidaan sijoittaa eri korkeudelle reaktorissa niin, että kiintoaine voidaan ohjata haluttuun kohtaan.Cooling ducts can be equipped with a cooling jacket I Ia if the solid to be returned to the reactor is to be cooled. Pa I aisles can be equipped with a valve so that some of the ducts can be closed. The connection points of the feed channels can be placed at different heights in the reactor so that the solid can be directed to the desired location.
Keksintö ei ole rajoitettu esimerkkinä esitettyyn suoritusmuotoon vaan sitä voidaan muunnella ja soveltaa patenttivaatimuksen määrittelemän keksinnöllisen ajatuksen puitte i ssa.The invention is not limited to the exemplary embodiment but can be modified and applied within the scope of the inventive idea defined by the claim.
Claims (1)
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI844442A FI70528C (en) | 1984-06-01 | 1984-11-13 | Apparatus for separating solids in circulating bed reactor. |
GB858512035A GB8512035D0 (en) | 1984-11-13 | 1985-05-13 | Separating solid material in reactor |
AU42611/85A AU557224B2 (en) | 1984-06-01 | 1985-05-17 | Separating solids in a circulating fluidized bed reactor |
DE19853517986 DE3517986A1 (en) | 1984-06-01 | 1985-05-18 | DEVICE FOR SEPARATING SOLID MATERIAL IN A REACTOR WITH A CIRCULATING FLUID BED |
GB858512739A GB8512739D0 (en) | 1984-11-13 | 1985-05-20 | Separating solid material in bed reactor |
SE8502499A SE460951B (en) | 1984-06-01 | 1985-05-21 | DEVICE FOR SEPARATION OF SOLID MATERIALS IN REACTOR WITH CIRCULATING BED |
CA000482775A CA1258037A (en) | 1984-06-01 | 1985-05-30 | Apparatus for separating solids in a circulating fluidized bed reactor |
GB08513916A GB2159726B (en) | 1984-06-01 | 1985-06-03 | Apparatus for separating solid material in a circulating fluidized bed reactor |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI842202 | 1984-06-01 | ||
FI842202A FI842202A0 (en) | 1984-06-01 | 1984-06-01 | ANCILLATION OF THE FAST MATERIAL I REACTOR WITH CIRCULAR BEDD. |
FI844442 | 1984-11-13 | ||
FI844442A FI70528C (en) | 1984-06-01 | 1984-11-13 | Apparatus for separating solids in circulating bed reactor. |
Publications (4)
Publication Number | Publication Date |
---|---|
FI844442A0 FI844442A0 (en) | 1984-11-13 |
FI844442L FI844442L (en) | 1985-12-02 |
FI70528B FI70528B (en) | 1986-06-06 |
FI70528C true FI70528C (en) | 1987-11-25 |
Family
ID=26157613
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FI844442A FI70528C (en) | 1984-06-01 | 1984-11-13 | Apparatus for separating solids in circulating bed reactor. |
Country Status (6)
Country | Link |
---|---|
AU (1) | AU557224B2 (en) |
CA (1) | CA1258037A (en) |
DE (1) | DE3517986A1 (en) |
FI (1) | FI70528C (en) |
GB (1) | GB2159726B (en) |
SE (1) | SE460951B (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5171542A (en) * | 1984-03-20 | 1992-12-15 | A. Ahlstrom Corporation | Circulating fluidized bed reactor |
US4900516A (en) * | 1984-06-01 | 1990-02-13 | A. Ahlstrom Corporation | Fluidized bed reactor |
FI86105C (en) * | 1985-11-19 | 1992-07-10 | Ahlstroem Oy | Method and apparatus for controlling the operation of a fluidized bed reactor |
WO1987003668A1 (en) * | 1985-12-09 | 1987-06-18 | A. Ahlstrom Corporation | A circulating fluidized bed reactor and a method of separating solid material from the flue gases |
US4869207A (en) * | 1987-07-13 | 1989-09-26 | A. Ahlstrom Corporation | Circulating fluidized bed reactor |
US5174799A (en) * | 1990-04-06 | 1992-12-29 | Foster Wheeler Energy Corporation | Horizontal cyclone separator for a fluidized bed reactor |
DE4308103A1 (en) * | 1993-03-15 | 1994-09-22 | Buehler Ag | Fluidized bed |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI62468C (en) * | 1981-08-24 | 1983-01-10 | Ahlstroem Oy | VIRVELBAEDDSREAKTOR |
-
1984
- 1984-11-13 FI FI844442A patent/FI70528C/en not_active IP Right Cessation
-
1985
- 1985-05-17 AU AU42611/85A patent/AU557224B2/en not_active Ceased
- 1985-05-18 DE DE19853517986 patent/DE3517986A1/en active Granted
- 1985-05-21 SE SE8502499A patent/SE460951B/en not_active IP Right Cessation
- 1985-05-30 CA CA000482775A patent/CA1258037A/en not_active Expired
- 1985-06-03 GB GB08513916A patent/GB2159726B/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
SE8502499D0 (en) | 1985-05-21 |
FI844442L (en) | 1985-12-02 |
SE8502499L (en) | 1985-12-02 |
FI70528B (en) | 1986-06-06 |
GB2159726B (en) | 1988-03-02 |
SE460951B (en) | 1989-12-11 |
DE3517986A1 (en) | 1985-12-05 |
DE3517986C2 (en) | 1989-06-01 |
GB2159726A (en) | 1985-12-11 |
AU4261185A (en) | 1985-12-05 |
AU557224B2 (en) | 1986-12-11 |
CA1258037A (en) | 1989-08-01 |
GB8513916D0 (en) | 1985-07-03 |
FI844442A0 (en) | 1984-11-13 |
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Legal Events
Date | Code | Title | Description |
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MM | Patent lapsed | ||
MM | Patent lapsed |
Owner name: A. AHLSTROEM OSAKEYHTIOE |