SU474665A1 - Shaft furnace fluidized bed - Google Patents
Shaft furnace fluidized bedInfo
- Publication number
- SU474665A1 SU474665A1 SU1925327A SU1925327A SU474665A1 SU 474665 A1 SU474665 A1 SU 474665A1 SU 1925327 A SU1925327 A SU 1925327A SU 1925327 A SU1925327 A SU 1925327A SU 474665 A1 SU474665 A1 SU 474665A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- fluidized bed
- furnace
- shaft furnace
- gas
- burners
- Prior art date
Links
- 239000007789 gas Substances 0.000 description 15
- 239000000463 material Substances 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 7
- 238000010304 firing Methods 0.000 description 4
- 239000004927 clay Substances 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 239000013590 bulk material Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
Classifications
-
- 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
- B01J8/44—Fluidisation grids
-
- 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
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/16—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by suspending the powder material in a gas, e.g. in fluidised beds or as a falling curtain
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B20/00—Use of materials as fillers for mortars, concrete or artificial stone according to more than one of groups C04B14/00 - C04B18/00 and characterised by shape or grain distribution; Treatment of materials according to more than one of the groups C04B14/00 - C04B18/00 specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Expanding or defibrillating materials
- C04B20/02—Treatment
- C04B20/04—Heat treatment
- C04B20/06—Expanding clay, perlite, vermiculite or like granular materials
- C04B20/065—Expanding clay, perlite, vermiculite or like granular materials in fluidised beds
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Ceramic Engineering (AREA)
- Thermal Sciences (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Physics & Mathematics (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
1one
Изобретение относитс к устройствам, предназначенным дл осуществлени процесса термической обработки сыпучих материалов, например, из глинистых, вулканических и других пород в производсгве пористых заполнителей дл бетонов.The invention relates to devices for carrying out the process of heat treatment of bulk materials, for example, from clay, volcanic and other rocks in the production of porous aggregates for concrete.
Известны печи кип щего сло дл обжига сыпучих материалов с применением газообразного топлива, разделенные на зоны подогрева , обжига и охлаждени и имеющие подину зоны обжига, набранную из горелок, выполненных с центральной газоподающей трубкой и периферийной воздухоподающей трубой .Fluid bed furnaces are known for firing bulk materials using gaseous fuels, divided into heating, firing and cooling zones and having a bottom burning zone recruited from burners made with a central gas supply tube and a peripheral air supply tube.
Однако в указанной печи материал между горелками залегает значительно выше уровн сопел. При обжиге в такой печи сыпучих материалов , обладающих свойством спекатьс , например, из глинистых, вулканических и других пород, в процессе обжига в местах залегани материал спекаетс , что приводит к прекращению технологического процесса.However, in this furnace, the material between the burners lies considerably above the level of the nozzles. When firing in such a furnace, bulk materials that have the property of sintering, for example, from clay, volcanic and other rocks, in the firing process in places of bedding, the material is sintered, which leads to the termination of the technological process.
Цель изобретени - уменьшить залегание материала между горелками выше уровн сопел , предотвратив тем самым его спекание. The purpose of the invention is to reduce the occurrence of material between the burners above the level of the nozzles, thereby preventing its sintering.
Это достигаетс тем, что горелки расположены на подине равномерно, и воздухоподающа труба каждой горелки выполнена с диффузором , а газоподающа - с конической насадкой , образующей с диффузором кольцевой This is achieved by the fact that the burners are uniformly located on the hearth, and the air supply tube of each burner is made with a diffuser, and the gas supply tube with a conical nozzle, which forms an annular
канал и имеющей центральное отверстие дл выхода газа, причем зона обжига печи в месте установки подины выполнена конической с расположением выгрузочной течки на верхнем уровне кип щего сло .a channel and having a central opening for the gas outlet, the burning zone of the furnace at the place of installation of the bottom is made conical with the location of the discharge chute at the upper level of the fluidized bed.
На фиг. 1 изображена предлагаема печь, продольный разрез; на фиг. 2 - газогорелочное устройство; на фиг. 3 - узел I на фиг. 2.FIG. 1 shows the proposed furnace, longitudinal section; in fig. 2 - gas burner device; in fig. 3 shows the node I in FIG. 2
Печь представл ет собой вертикальную футерованную шахту , разделенную перегородкой 2 на две зоны: верхн - термоподготовки , нижн - обжига. В зоне термоподготовки установлена перфорированна подина 3. Печь снабжена футерованным циклоном 4, внешним перетоком 5 с клапанным затвором, системой коллекторов 6, газогорелочным устройством 7 и выгрузочной течкой 8 из зоны обжига.The furnace is a vertical lined shaft, divided by partition 2 into two zones: the top is thermal treatment, the bottom is roasting. In the heat treatment zone, a perforated bottom 3 is installed. The furnace is equipped with a lined cyclone 4, an external overflow 5 with a valve gate, a collector system 6, a gas-burning device 7 and a discharge chute 8 from the burning zone.
Газогорелочное устройство выполнено в виде набора секций, кажда из которых имеет корпус 9, газовый коллектор 10 п равномерно распределенные горелки (узел I). У каждой горелки газоподающа труба снабл ена конической насадкой 11 с центральным каналом 12 дл выхода газа и расположена коаксиально внутри воздухоподающей трубы, снабженной диффузором 13, образующим с конической насадкой 11 кольцевой канал дл выхода воздуха.The gas burner device is made in the form of a set of sections, each of which has a housing 9, a gas collector 10 n evenly distributed burners (node I). Each burner has a gas supply pipe equipped with a conical nozzle 11 with a central channel 12 for gas outlet and is located coaxially inside an air supply pipe equipped with a diffuser 13, which forms an annular air channel with the conical nozzle 11.
Печь может быть выполнена одно-, двух и многозонной, круглой, эллиптической, пр моугольной или любой другой формы.The furnace can be of one, two or multi-zone, round, elliptical, rectangular or any other shape.
Печь работает следующим образом.The furnace works as follows.
Дробленый или гранулированный материал, например, дроблена глина, подаетс в зону термоподготовки печи, где нагреваетс за счет тепла газов, отход щих из зоны обжига. Из зоны термоподготовки материал но внешнему перетоку 5 поступает в зону обжига, где нагреваетс до пиропластического состо ни и вспучивани за счет тепла, выдел ющегос при сгорании газообразного топлива, непосредственно в кип щем слое материала. Вспученный материал выгружаетс из печи через течку 8.Crushed or granulated material, such as crushed clay, is fed to the heat treatment zone of the furnace, where it is heated by the heat from the gases coming from the burning zone. From the heat treatment zone, the material but the external overflow 5 enters the burning zone, where it is heated to the pyroplastic state and swelling due to the heat generated during the combustion of the gaseous fuel directly in the fluidized bed of the material. The expanded material is discharged from the furnace through the chute 8.
Газ и воздух через систему коллекторов 6 и подовое газогорелочное устройство 7 подаютс в зону обжига, где происходит их смещение и сгорание газообразного топлива. Отход щие газы из зоны обжига после очистки в футерованном циклоне 4 через решетку подаютс в зону термоподготовки.Gas and air through the system of collectors 6 and the bottom gas burner device 7 is fed into the burning zone, where they are displaced and the gaseous fuel is burned. Exhaust gases from the burning zone after cleaning in the lined cyclone 4 are fed through a grid to the heat treatment zone.
Предмет изобретени Subject invention
Шахтна печь кип щего сло дл обжига сыпучего материала, содержаща зоны подогрева и обжига с подиной, набранной из горелок , выполненных с центральной газоподающей трубой, периферийной воздухоподающей трубой, отличающа с тем, что, с целью предотвращени спекани материала, горелки распределены по площади подины равномерно, воздухоподающа труба каждой горелки выполнена с диффузором, а газоподающа - с конической насадкой, образующей с диффузором кольцевой канал и имеющей центральное отверстие дл выхода газа, причем зона обжига печи в месте установки подины выполнена конической с расположением выгрузочной течки на верхнем уровне кип щего сло .The fluidized bed shaft furnace for calcining the bulk material, comprising heating and hearth burning zones, recruited from burners made with a central gas supply pipe, a peripheral air supply pipe, characterized in that, to prevent sintering of the material, the burners are evenly distributed throughout the bottom area , the air supply tube of each burner is made with a diffuser, and the gas supply tube is made with a conical nozzle, which forms an annular channel with a diffuser and has a central opening for the exit of gas, and the burning zone is chi at the installation site of the hearth is conical with unloading chutes located at the upper level of the fluidized bed.
ЦШ ЛД11ППППП|10ПП 1 zziHr::; TsSh LD11PPPP | 10PP 1 zziHr ::;
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1925327A SU474665A1 (en) | 1973-06-13 | 1973-06-13 | Shaft furnace fluidized bed |
| DE19742427958 DE2427958C3 (en) | 1973-06-13 | 1974-06-10 | Burners for fluidized bed furnaces |
| FR7420574A FR2233092A1 (en) | 1973-06-13 | 1974-06-13 | Foam aggregates for cement - made in fluid bed kiln with direct fuel combustion, in fluid bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1925327A SU474665A1 (en) | 1973-06-13 | 1973-06-13 | Shaft furnace fluidized bed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU474665A1 true SU474665A1 (en) | 1975-06-25 |
Family
ID=20554630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU1925327A SU474665A1 (en) | 1973-06-13 | 1973-06-13 | Shaft furnace fluidized bed |
Country Status (3)
| Country | Link |
|---|---|
| DE (1) | DE2427958C3 (en) |
| FR (1) | FR2233092A1 (en) |
| SU (1) | SU474665A1 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2737079A1 (en) * | 1976-08-23 | 1978-03-09 | Gvnii Tsementnoj Promy | DEVICE FOR THE HEAT TREATMENT OF A BULK GOOD IN FLOATING CONDITION |
| DE3007711C2 (en) * | 1980-02-29 | 1987-01-02 | Kernforschungsanlage Jülich GmbH, 5170 Jülich | Inflow unit for a fluidized bed furnace |
| IT1188886B (en) * | 1980-12-24 | 1988-01-28 | Fata Europ Group | CALCINATION OVEN WITH A FLUIDIZED BED PARTICULARLY FOR THE RECOVERY OF SANDS USED IN FOUNDRY SHAPES AND SOULS |
| JPS57170823A (en) * | 1981-04-09 | 1982-10-21 | Nippon Carbide Ind Co Ltd | Fluidized roasting method and apparatus |
| DE3151164C2 (en) * | 1981-12-23 | 1985-02-07 | Deutsche Perlite Gmbh, 4600 Dortmund | Device for expanding perlite, vermiculite and similar expanded material |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1141934B (en) * | 1960-08-25 | 1962-12-27 | Veit Dennert K G | Treatment chamber that can be heated by at least one burner for the preparation of bulky goods |
| FR1504435A (en) * | 1965-11-24 | 1967-12-08 | Siderurgie Fse Inst Rech | Improvements in fluidization treatment processes and implementation device |
| DE1758244B1 (en) * | 1968-04-27 | 1971-05-19 | Metallgesellschaft Ag | DEVICE FOR EQUAL DOSED SUPPLY OF FUEL AND AIR INTO A FLUID BED |
| FR1595470A (en) * | 1968-12-24 | 1970-06-08 | ||
| US3737283A (en) * | 1971-11-26 | 1973-06-05 | Fuller Co | Fluidized solids reactor |
-
1973
- 1973-06-13 SU SU1925327A patent/SU474665A1/en active
-
1974
- 1974-06-10 DE DE19742427958 patent/DE2427958C3/en not_active Expired
- 1974-06-13 FR FR7420574A patent/FR2233092A1/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| DE2427958C3 (en) | 1981-06-04 |
| DE2427958B2 (en) | 1980-10-02 |
| FR2233092A1 (en) | 1975-01-10 |
| FR2233092B1 (en) | 1976-12-24 |
| DE2427958A1 (en) | 1975-01-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| SU629904A3 (en) | Device for heat treatment of fine grainy material | |
| US3285590A (en) | Down draft vertical kiln system | |
| SU474665A1 (en) | Shaft furnace fluidized bed | |
| US3404199A (en) | Heating process in a rotary kiln | |
| SU1145228A2 (en) | Furnace for roasting fine-grain material in fluidized bed | |
| US2590202A (en) | Material discharge mechanism | |
| US3766663A (en) | Preheater for lime kiln | |
| US2512442A (en) | Solid material heating apparatus | |
| US3511485A (en) | Furnaces for processing expandable volcanic rock | |
| SU141171A1 (en) | Multizone shaft furnace | |
| USRE30469E (en) | Preheater for lime kiln | |
| RU1796850C (en) | Regenerative shaft kiln | |
| SU393561A1 (en) | BIBLE. '.' YUTEKA | |
| SU1366830A1 (en) | Shaft furnace | |
| SU135092A1 (en) | Device for heating gases and air with a suspended bed | |
| SU10699A1 (en) | Shaft furnace for firing materials at low temperatures | |
| SU1212549A1 (en) | Apparatus with fluidized bed for thermal processing of high-ash coal | |
| SU966062A1 (en) | Method for roasting cement clinker in rotary kiln | |
| SU1362904A1 (en) | Shaft furnace | |
| SU432321A1 (en) | FURNACE FOR HEATING SILES | |
| RU2066817C1 (en) | Shaft furnace | |
| SU924478A1 (en) | Cyclone shaft furnace | |
| SU118755A1 (en) | Cement clinker, limestone and other granular and granular materials kiln in a fluidized bed | |
| SU1032312A1 (en) | Plant for roasting granular material | |
| SU1186921A1 (en) | Apparatus for fluidized bed roasting of polydisperse material |