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SU474665A1 - Shaft furnace fluidized bed - Google Patents

Shaft furnace fluidized bed

Info

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
Application number
SU1925327A
Other languages
Russian (ru)
Inventor
Ализакир Алигады Оглы Ахундов
Николай Борисович Кондуков
Харлампий Сергеевич Воробьев
Валентин Матвеевич Дементьев
Борис Соломонович Фарбер
Алексей Александрович Зеленов
Владимир Александрович Логвинов
Original Assignee
Государственный Всесоюзный Научно-Исследовательский Институт Строительных Материалов И Конструкций
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Государственный Всесоюзный Научно-Исследовательский Институт Строительных Материалов И Конструкций filed Critical Государственный Всесоюзный Научно-Исследовательский Институт Строительных Материалов И Конструкций
Priority to SU1925327A priority Critical patent/SU474665A1/en
Priority to DE19742427958 priority patent/DE2427958C3/en
Priority to FR7420574A priority patent/FR2233092A1/en
Application granted granted Critical
Publication of SU474665A1 publication Critical patent/SU474665A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical 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
    • B01J8/44Fluidisation grids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/16Processes 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical 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
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B20/00Use 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
    • C04B20/02Treatment
    • C04B20/04Heat treatment
    • C04B20/06Expanding clay, perlite, vermiculite or like granular materials
    • C04B20/065Expanding 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 ::;

SU1925327A 1973-06-13 1973-06-13 Shaft furnace fluidized bed SU474665A1 (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

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

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