CN106277856B - Coal-fired lime sleeve kiln combusting room device and its Slagoff method - Google Patents

Coal-fired lime sleeve kiln combusting room device and its Slagoff method Download PDF

Info

Publication number
CN106277856B
CN106277856B CN201610686905.8A CN201610686905A CN106277856B CN 106277856 B CN106277856 B CN 106277856B CN 201610686905 A CN201610686905 A CN 201610686905A CN 106277856 B CN106277856 B CN 106277856B
Authority
CN
China
Prior art keywords
flue
ash
combustion chamber
coal
dust retainer
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.)
Active
Application number
CN201610686905.8A
Other languages
Chinese (zh)
Other versions
CN106277856A (en
Inventor
张震
韦传稳
马明春
王欣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Great Huan Group Co Ltd
Original Assignee
Great Huan Group Co Ltd
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 Great Huan Group Co Ltd filed Critical Great Huan Group Co Ltd
Priority to CN201610686905.8A priority Critical patent/CN106277856B/en
Publication of CN106277856A publication Critical patent/CN106277856A/en
Application granted granted Critical
Publication of CN106277856B publication Critical patent/CN106277856B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • C04B2/00Lime, magnesia or dolomite
    • C04B2/10Preheating, burning calcining or cooling
    • C04B2/12Preheating, burning calcining or cooling in shaft or vertical furnaces
    • 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
    • C04B2/00Lime, magnesia or dolomite
    • C04B2/10Preheating, burning calcining or cooling
    • C04B2/108Treatment or selection of the fuel therefor
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/40Production or processing of lime, e.g. limestone regeneration of lime in pulp and sugar mills

Abstract

The invention discloses a kind of coal-fired lime sleeve kiln combusting room device and its Slagoff methods, the combusting room device includes the cannular combustion chamber being obliquely installed, chamber temperature detector is equipped at the top of cannular combustion chamber, cannular combustion chamber bottom is equipped with diversion trench, diversion trench lower end is equipped with ash discharging hole, collection apparatus for ash is equipped with below ash discharging hole, collecting apparatus for ash includes flue-dust retainer, flue-dust retainer side wall is equipped with cool air hose, flue-dust retainer temperature monitor is equipped with inside flue-dust retainer, flue-dust retainer lower end is equipped with ash gate, and ash gate connects revolving plow reclaimer.The combusting room device Slagoff method: during coal dust is burnt, ash content in coal dust is fired into molten slag and falls into diversion trench, then it is fallen into flue-dust retainer through ash discharging hole, cold front heavy rain is passed through as solid, powdery and scoriform object by cool air hose in flue-dust retainer, is then discharged by flue-dust retainer lower end revolving plow reclaimer.The problem of clearing up is difficult to after slagging and slagging in combustion chamber when the present invention solves sleeve kiln fire coal.

Description

Coal-fired lime sleeve kiln combusting room device and its Slagoff method
Technical field
The present invention relates to lime sleeve kiln coal combustion technology field, especially a kind of coal-fired lime with slag tap function Sleeve kiln combusting room device and its Slagoff method.
Background technique
For annular lime kiln because occupied area is small, finished product activity of lime is high, and the porosity is high, the raw low advantage of burning rate and it is wide The general lime production enterprise for being applied to metallurgy, chemical industry and building materials field.The traditional fuel of annular lime kiln is coal gas, such as coke-oven coal Gas, coal gas of converter or blast furnace coke oven mixed gas etc..In recent years, with the latent and energy saving and cost lowering requirement of deep-cutting of industry, and permitted Multiple enterprises are used for lime production without enough coal gas because of the limitation of area surroundings.Therefore, lime production producer is for annular Sleeve kiln is persistently increased using coal dust as the attention rate of fuel, and the country has also gradually started to annular lime kiln coal combustion technology Theoretical Proof and practical exploration.
Annular lime kiln fire coal is main problem is encountered that slagging in combustion chamber in production.Coal dust is sprayed into through burner to burn Burning, the high temperature for generation of burning are softened or melted the ash content in coal dust rapidly after indoor, and a part of ash content is attached to burning Cooling and solidifying forms slagging on the resistance to material in room, builds up from level to level in this way, indoor slagging amount of burning is more and more.
It needs to stop burner combustion by manually or mechanically mode scarfing cinder, waits burning room temperature to reduce, the knot of softening After slag becomes fragile, it can clear up.This manner of cleaning up influences the continuous production operation in limekiln, and to the resistance to material service life of combustion chamber There is adverse effect.And if not clearing up combustion chamber for a long time, on the one hand, combustion chamber ventilation resistance increases, flow field is destroyed, and influences lime The calcine technology of sleeve kiln;On the other hand, flame flows into kiln after melting part coal ash burning, and slag is easy to be formed on resistance to material and hang Wall and lime stone is caused to agglomerate, influence lime quality, once causing viscous kiln, will also have to stop kiln processing agglomeration.
Summary of the invention
Goal of the invention: it is difficult to after slagging and slagging in combustion chamber when the invention aims to solve sleeve kiln fire coal The problem of cleaning, provides a kind of coal-fired lime sleeve kiln combusting room device and its Slagoff method with slag tap function.
To achieve the goals above, present invention employs the following technical solutions: a kind of fire coal lime sleeve kiln combustion chamber Device, including burner block, burning chamber shell, cannular combustion chamber, burner block are arranged in burning chamber shell end, and burner block is equipped with Burner, cannular combustion chamber are arranged on the inside of burning chamber shell;The cannular combustion chamber is obliquely installed, and is equipped at the top of cannular combustion chamber Chamber temperature detector, cannular combustion chamber bottom offer the diversion trench of strip along central axes direction, and diversion trench lower end is set There is the ash discharging hole through burning chamber shell, collection apparatus for ash is equipped with below ash discharging hole, collection apparatus for ash includes the flue-dust retainer being vertically arranged, Flue-dust retainer upper end connects ash discharging hole, and flue-dust retainer side wall is equipped with cool air hose, and cool air hose is equipped with flowmeter and electric control valve, flue-dust retainer Inside is equipped with flue-dust retainer temperature monitor, and flue-dust retainer lower end is equipped with ash gate, and ash gate connects revolving plow reclaimer.
Further, the cannular combustion chamber is equipped with driving air duct close to one end of burner block, and driving air duct is in volute, drives The air inlet in dynamic air duct is located on burning chamber shell, drives the air outlet in air duct to be located at cannular combustion chamber, and drive air duct Section is gradually become smaller by air inlet to air outlet.
Further, the ash discharging hole flare, the big mouth down of ash discharging hole.
Further, cannular combustion chamber central axes angle with horizontal plane is 10 °.
According to the Slagoff method of above-mentioned combusting room device: spraying into the mistake that cannular combustion chamber burns through burner in coal dust Cheng Zhong, the ash content in coal dust are fired into molten slag and fall into diversion trench, and the ash discharging hole then through diversion trench lower end is fallen into In flue-dust retainer, molten slag is passed through cold front heavy rain as solid, powdery and scoriform object by cool air hose in flue-dust retainer, then passes through The discharge of flue-dust retainer lower end revolving plow reclaimer.
Further, the ash content ash fusion point in the coal dust is less than 1200 DEG C, fineness of pulverized coal R75 < 10%, coal dust firing In the process, cannular combustion chamber temperature is not less than 1200 DEG C.
The utility model has the advantages that (1) present invention can be achieved in coal-fired lime sleeve kiln combustion chamber the online slag tap of slagging and from Cleaning;(2) compared with traditional sleeve kiln combustion chamber, slagging in manual cleaning combustion chamber is not needed, does not need to stop kiln cleaning yet Slagging improves the production operational availability of sleeve kiln;(3) collection provided with coal ash melt cinder and outer arranging device, melt cinder may not flow into Wall built-up and sizing are caused in kiln, but is expelled directly out outside kiln, and any adverse effect is not generated to production;(4) the coal ash knot collected Slag be solid particulate matter or powder, it is easy to clean;(5) have to temperature in chamber temperature, coal dust ash fusion point sum aggregate ash bucket clear It is required that realizing the automation control of combustion chamber liquid deslagging.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of combusting room device of the present invention;
Fig. 2 is the structural schematic diagram of diversion trench;
Fig. 3 is driving air channel structure schematic diagram;
Fig. 4 is the structural schematic diagram for collecting apparatus for ash.
In figure: 1- burner, 2- burner block, 3- burning chamber shell, the resistance to material of 4-, 5- drive air duct, 5-1- air inlet, and 5-2- goes out Air port, 6- cannular combustion chamber, 7- diversion trench, 8- chamber temperature detector, 9- ash discharging hole, 10- collection apparatus for ash, 11- impeller are given Material machine, 12- flue-dust retainer, 13- cool air hose, 14- flowmeter, 15- flue-dust retainer temperature monitor, 16- electric control valve, 17- deslagging Door, 18- kiln shell.
Specific embodiment:
Further explanation is done to the present invention with reference to the accompanying drawing.
As illustrated in fig. 1 and 2, a kind of coal-fired lime sleeve kiln combusting room device of the invention, including burner block 2, combustion chamber Shell 3, cannular combustion chamber 6.Burning chamber shell 3 is fixed on the kiln shell 18 of sleeve kiln.Burner block 2 is arranged in burning chamber shell 3 End, burner block 2 are equipped with burner 1, and the setting of cannular combustion chamber 6 is in 3 inside of burning chamber shell, and cannular combustion chamber 6 is close to burner One end of brick 2 is equipped with driving air duct 5.3 outer wall of burning chamber shell and 6 inner wall of cannular combustion chamber are equipped with resistance to material 4.
The cannular combustion chamber 6 is obliquely installed, and 6 central axes angle with horizontal plane of cannular combustion chamber is 10 °.Cannular combustion chamber The resistance to material 4 at 6 tops is equipped with chamber temperature detector 8, opens up on the resistance to material 4 of 6 bottom of cannular combustion chamber along central axes direction There is the diversion trench 7 of strip, 7 lower end of diversion trench is equipped with the ash discharging hole 9 through burning chamber shell 3, institute close to the position of kiln shell 18 State 9 flare of ash discharging hole, the big mouth down of ash discharging hole 9.Collection apparatus for ash 10 is equipped with below ash discharging hole 9.
As shown in figure 3, the cannular combustion chamber 6 is equipped with driving air duct 5 close to one end of burner block 2, driving air duct 5 is in snail The air inlet 5-1 of shape, driving air duct 5 is located on burning chamber shell 3, and the air outlet 5-2 in driving air duct 5 is located at cannular combustion chamber 6, And the section in air duct 5 is driven to be gradually become smaller by air inlet 5-1 to air outlet 5-2.After external wind introduces driving air duct 5, along The rotation of volute line accelerates, and then passes to cannular combustion chamber 6, the flame in cannular combustion chamber 6 can be wrapped up and allow combustion air and fire Flame is rotated in cannular combustion chamber 6, to facilitate coal dust full combustion.
As shown in figure 4, the collection apparatus for ash 10 includes the flue-dust retainer 12 being vertically arranged, 12 upper end of flue-dust retainer connects ash discharging hole 9,12 side wall of flue-dust retainer is equipped with cool air hose 13, and cool air hose 13 is equipped with flowmeter 14 and electric control valve 16, in flue-dust retainer 12 Portion is equipped with flue-dust retainer temperature monitor 15, and 12 lower end of flue-dust retainer is equipped with ash gate 17, and ash gate 17 connects revolving plow reclaimer 11.
When coal dust is when cannular combustion chamber 6 is burnt, generation negative pressure in cannular combustion chamber 6, outside air can be through cold wind Pipe 13 enters flue-dust retainer 12, and temperature in flue-dust retainer 12 can be monitored in real time in flue-dust retainer temperature monitor 15, by cool air hose 13 Gas flow can be adjusted in real time according to temperature in flue-dust retainer 12.Revolving plow reclaimer 11 uses sealed construction, it is ensured that without outer Boundary's air is entered in flue-dust retainer 12 by revolving plow reclaimer 11.
According to the Slagoff method of above-mentioned combusting room device: spraying into the mistake that cannular combustion chamber 6 burns through burner 1 in coal dust Cheng Zhong, the ash content in coal dust are fired into molten slag and fall into diversion trench 7, and the ash discharging hole 9 then through 7 lower end of diversion trench is fallen Entering in flue-dust retainer 12, molten slag, which is passed through cold front heavy rain by cool air hose 13 in flue-dust retainer 12, becomes solid, powdery and scoriform object, Then it is discharged by 12 lower end revolving plow reclaimer 11 of flue-dust retainer.In order to guarantee that the ash content in coal dust can in cannular combustion chamber 6 Sufficiently melting, the ash content ash fusion point in the coal dust is less than 1200 DEG C, fineness of pulverized coal R75 < 10%, during coal dust firing, 6 temperature of cannular combustion chamber is not less than 1200 DEG C.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered It is considered as protection scope of the present invention.

Claims (6)

1. a kind of fire coal lime sleeve kiln combusting room device, including burner block (2), burning chamber shell (3), cannular combustion chamber (6), Burner block (2) setting is equipped with burner (1) in burning chamber shell (3) end, burner block (2), and cannular combustion chamber (6) setting is being fired It burns on the inside of room housing (3);It is characterized by: the cannular combustion chamber (6) is obliquely installed, combustion is equipped at the top of cannular combustion chamber (6) It burns room temperature detector (8), cannular combustion chamber (6) bottom offers the diversion trench (7) of strip, diversion trench along central axes direction (7) lower end is equipped with the ash discharging hole (9) through burning chamber shell (3), is equipped with collection apparatus for ash (10) below ash discharging hole (9), collects ash dress Setting (10) includes the flue-dust retainer (12) being vertically arranged, and flue-dust retainer (12) upper end connects ash discharging hole (9), and flue-dust retainer (12) side wall is equipped with Cool air hose (13), cool air hose (13) are equipped with flowmeter (14) and electric control valve (16), are equipped with flue-dust retainer inside flue-dust retainer (12) Temperature monitor (15), flue-dust retainer (12) lower end are equipped with ash gate (17), and ash gate (17) connects revolving plow reclaimer (11).
2. a kind of coal-fired lime sleeve kiln combusting room device according to claim 1, it is characterised in that: the tubular burning Room (6) is equipped with driving air duct (5) close to the one end of burner block (2), and driving air duct (5) is in volute, drives the air inlet of air duct (5) (5-1) is located on burning chamber shell (3), and the air outlet (5-2) of driving air duct (5) is located at cannular combustion chamber (6), and drives wind The section in road (5) is gradually become smaller by air inlet (5-1) to air outlet (5-2).
3. a kind of coal-fired lime sleeve kiln combusting room device according to claim 1 or 2, it is characterised in that: the ash discharge Mouth (9) flare, the big mouth down of ash discharging hole (9).
4. a kind of coal-fired lime sleeve kiln combusting room device according to claim 3, it is characterised in that: the tubular burning Room (6) central axes angle with horizontal plane is 10 °.
5. the Slagoff method of combusting room device according to claim 1, it is characterised in that: sprayed into coal dust through burner (1) During cannular combustion chamber (6) is burnt, the ash content in coal dust is fired into molten slag and falls into diversion trench (7), Then the ash discharging hole (9) through diversion trench (7) lower end is fallen into flue-dust retainer (12), and molten slag is in flue-dust retainer (12) by cool air hose (13) cold front heavy rain is passed through as solid, powdery and scoriform object, is then arranged by flue-dust retainer (12) lower end revolving plow reclaimer (11) Out.
6. the Slagoff method of combusting room device according to claim 5, it is characterised in that: the ash content ash in the coal dust is molten O'clock less than 1200 DEG C, fineness of pulverized coal R75 < 10%, during coal dust firing, cannular combustion chamber (6) temperature is not less than 1200 DEG C.
CN201610686905.8A 2016-08-17 2016-08-17 Coal-fired lime sleeve kiln combusting room device and its Slagoff method Active CN106277856B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610686905.8A CN106277856B (en) 2016-08-17 2016-08-17 Coal-fired lime sleeve kiln combusting room device and its Slagoff method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610686905.8A CN106277856B (en) 2016-08-17 2016-08-17 Coal-fired lime sleeve kiln combusting room device and its Slagoff method

Publications (2)

Publication Number Publication Date
CN106277856A CN106277856A (en) 2017-01-04
CN106277856B true CN106277856B (en) 2019-03-08

Family

ID=57660464

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610686905.8A Active CN106277856B (en) 2016-08-17 2016-08-17 Coal-fired lime sleeve kiln combusting room device and its Slagoff method

Country Status (1)

Country Link
CN (1) CN106277856B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106705035B (en) * 2017-01-16 2019-07-12 大峘集团有限公司 A kind of sleeve kiln upper combustion chamber coal dust combustion method and device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN205893099U (en) * 2016-08-17 2017-01-18 大峘集团有限公司 Coal -fired lime sleeve kiln combustor device

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2050929U (en) * 1989-01-04 1990-01-10 东北工学院 Cyclone combustion furnace for coal power
DE19843820A1 (en) * 1998-09-24 2000-03-30 Adolf Schmidt Process for operating a shaft kiln for burning limestone uses natural gas, heating oil or coal dust as fuel in two combustion periods
CN201940176U (en) * 2011-03-04 2011-08-24 湖南湘达环保工程有限公司 Double-alkali integrated device for flue gas desulfurization, regeneration, separation and slag discharge
CN102875037A (en) * 2012-10-23 2013-01-16 石家庄市新华工业炉有限公司 Ash discharging system for sleeve kiln
CN104058608B (en) * 2014-06-15 2016-04-06 石家庄新华能源环保科技股份有限公司 A kind of shaft furnace of partition heated material

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN205893099U (en) * 2016-08-17 2017-01-18 大峘集团有限公司 Coal -fired lime sleeve kiln combustor device

Also Published As

Publication number Publication date
CN106277856A (en) 2017-01-04

Similar Documents

Publication Publication Date Title
CN100567526C (en) The method and system of heterogeneity dust separation in the stainless steel smelting process
CN201242342Y (en) Shaft kiln
CN103822357A (en) Horizontal pulverized coal organic heat carrier boiler
CN106277856B (en) Coal-fired lime sleeve kiln combusting room device and its Slagoff method
CN206973576U (en) Whiz device and the saliferous dangerous waste incinerator with whiz device
CN205893099U (en) Coal -fired lime sleeve kiln combustor device
CN104561594A (en) Tin smelting liquation furnace
CN102121788A (en) Smelting furnace
CN101644535A (en) Smelting furnace
CN203771690U (en) Horizontal coal dust organic heat carrier boiler
CN201565226U (en) System for dedusting smoke discharged in smelting outside furnace
CN207091486U (en) Flash Smelting Furnace flue
CN111074019B (en) Liquid slag dry-type granulating and waste heat recovering device with slag wool shearing and crushing functions and operation method thereof
CN207507183U (en) A kind of flue gas processing device for cast stone smelting furnace
CN104197733B (en) Regenerative cycles device in Gas heating furnace high-temperature burns carbon distribution device and technique
CN206875938U (en) A kind of energy-saving, environment-friendly and high-efficiency blast-heating cupola
CN206709610U (en) The combustion gas smelting furnace of continuous production high temperature rock/mineral wool raw materials liquation
CN214891325U (en) Hot-blast furnace with layered sealing structure for slag micro powder production
CN109579523A (en) A kind of modified natural gas heat accumulated type lead-melting furnace
CN2711660Y (en) Hot air cupola
CN205825067U (en) Rotating type impeller slag removal mechanism
CN204718364U (en) Many rows combustion gas melting shaft furnace
CN204474737U (en) Tin smelts liquating furnace
CN107726349A (en) Biomass combustion boiler nozzle and ashes cooling system
CN203518553U (en) Rotary kiln with thermal circulation function

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant