CN104803618B - annular lime shaft kiln - Google Patents

annular lime shaft kiln Download PDF

Info

Publication number
CN104803618B
CN104803618B CN201510205835.5A CN201510205835A CN104803618B CN 104803618 B CN104803618 B CN 104803618B CN 201510205835 A CN201510205835 A CN 201510205835A CN 104803618 B CN104803618 B CN 104803618B
Authority
CN
China
Prior art keywords
toroidal cavity
outer ring
ring wall
combustion
ringwall
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
CN201510205835.5A
Other languages
Chinese (zh)
Other versions
CN104803618A (en
Inventor
张玉宝
吴波
徐鹏
姜海
高勇
杨艳
郭玉刚
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.)
Zibo Is Kiln Engineering Finite Responsible Co Incomparably
Original Assignee
Zibo Is Kiln Engineering Finite Responsible Co Incomparably
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 Zibo Is Kiln Engineering Finite Responsible Co Incomparably filed Critical Zibo Is Kiln Engineering Finite Responsible Co Incomparably
Priority to CN201510205835.5A priority Critical patent/CN104803618B/en
Publication of CN104803618A publication Critical patent/CN104803618A/en
Application granted granted Critical
Publication of CN104803618B publication Critical patent/CN104803618B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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

Landscapes

  • Furnace Details (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Abstract

A kind of annular lime shaft kiln, including kiln body, described kiln body is made up of outer ring wall and interior ringwall, toroidal cavity is formed between inside and outside ringwall, connection outer ring wall and the lintel of interior ringwall it is provided with in toroidal cavity, toroidal cavity is divided into the position being in burning zone on preheating zone, burning zone and cooling zone, outer ring wall and interior ringwall to be equipped with burner from top to bottom.The upper end of described toroidal cavity is provided with material-feeding mechanism, and the bottom of toroidal cavity is provided with discharging mechanism, and the outside of described inside and outside ringwall is provided with feed mechanism, combustion-supporting mechanism, cooling body and waste gas dedusting system.This lime shaft kiln uses the loop configuration being made up of inside and outside ringwall, it is easy to being uniformly distributed of air-flow in kiln body, it is easy to uniform calcination and the multiaspect calcining of lime stone, avoid sizing phenomenon, there is the features such as production efficiency high, energy consumption is low, environmental protection, operation is safe, simple to operate, floor space is little, small investment.

Description

Annular lime shaft kiln
Technical field
The present invention relates to a kind of equipment generating quick lime for calcined limestone, belong to lime burning equipment technical field.
Background technology
Quick lime is to be generated by calcined limestone, traditional production technology be lime stone and fuel load limekiln (if gas Fuel is sent into through pipeline and burner) start to decompose to 850 degree after preheating, complete to calcine to 1200 degree, more after cooling, Unload outside kiln discharge.Limekiln mainly by kiln body, feeding device, distribution device, burner, ash-discharging device, dust arrester and Electric control gears etc. form.Applying most common is shaft furnace.The usage factor of common shaft furnace is below 50%, and power consumption height, production is imitated Rate is low.
Therefore the limekiln that some production efficiencys are higher is occurred in that, " single thorax as disclosed in Chinese patent literature CN103359958A Negative pressure, full-course dust-free production type double-hearth lime kiln ", CN102557492A disclosed " a kind of heat accumulating type double-hearth lime kiln " with And CN102701610A is disclosed " Concurrent flow type double-hearth limekiln ", it is to use two burner hearths calcined limestone simultaneously, but its Energy consumption does not reduce, and increases floor space simultaneously.
CN103641338B disclosed " a kind of to burning formula sleeve lime kiln ", including kiln body feed system, limekiln feeding system System, kiln body outer sleeve, kiln body inner sleeve, inside and outside to burn formula burner group, annular air cooler, multipoint mode seal ash hoist Group, finished product ash silo and finished product ash conveyer;Described kiln body feed system is arranged at the top of kiln body outer sleeve, itself and lime Kiln feeding system docks mutually;Described kiln body inner sleeve is arranged in kiln body outer sleeve, forms an annular burning district between the two; Inside and outside described, burning formula burner group is arranged in annular burning district;Described annular air cooler is arranged on bottom annular burning district; Described multipoint mode seals ash discharge unit and is arranged on bottom annular air cooler;Described finished product ash silo is arranged on multipoint mode and seals Bottom ash unit, dock mutually with finished product ash conveyer bottom it.Although this uses tube-in-tube structure, tool to burning formula sleeve lime kiln There is plurality of advantages, but still have much room for improvement in terms of energy-conservation, calcining homogeneity and efficiency.
Summary of the invention
The deficiency existed for existing limekiln technology, the present invention proposes the annular lime that a kind of production efficiency is high, energy consumption is low and erects Kiln.
The annular lime shaft kiln of the present invention, by the following technical solutions:
This annular lime shaft kiln, including kiln body, described kiln body is made up of outer ring wall and interior ringwall, between interior ringwall and outer ring wall Forming toroidal cavity, be provided with connection outer ring wall and the lintel of interior ringwall in toroidal cavity, toroidal cavity is divided into pre-from top to bottom The position being in burning zone on the torrid zone, burning zone and cooling zone, outer ring wall and interior ringwall is equipped with burner.
Described lintel layered arrangement from top to bottom in toroidal cavity.The bottom of described lintel is provided with cavity.
The inwall of described outer ring wall and the outer wall of interior ringwall are provided with refractory lining.
Described burner is two rows interlaced arrangement, and the burner on outer ring wall and interior ringwall is to spray, and each row's burner was respectively positioned on Under beam.
The upper end of described toroidal cavity is provided with material-feeding mechanism, and the bottom of toroidal cavity is provided with discharging mechanism, described outer ring wall Outside be provided with feed mechanism, combustion-supporting mechanism, cooling body and waste gas dedusting system.
Described feed mechanism includes hoist engine, truck and loading guide, and truck is arranged on loading guide, and with hoist engine even Connect.
Described material-feeding mechanism includes feed bin, distributor chute and cloth valve, and feed bin is positioned at the lower section of loading guide upper end, feed bin Bottom is provided with distributor chute, and each distributor chute is equipped with cloth valve, and each distributor chute is connected to outer ring wall and inner ring Between wall, and connect with described toroidal cavity.
Described discharging mechanism includes discharging machine, discharging gate valve and middle ash silo, and discharging machine is distributed in the bottom of toroidal cavity, and Be connected between outer ring wall and interior ringwall, each discharging machine be respectively provided with a discharging gate valve, the lower end of each discharging machine all with Middle ash silo connects.
Described combustion-supporting mechanism includes combustion fan, heat exchanger and combustion-supporting pipeline, and combustion fan is connected with heat exchanger, and heat is handed over Parallel operation is connected to outside outer ring wall by combustion-supporting pipeline and at the burning zone in inner ring portion within the walls.
Described cooling body includes cooling blower and cooling pipe, and cooling blower is by the cooling zone of cooling pipe with toroidal cavity Connection.
Described waste gas dedusting system includes exhaust gas fan, deduster and exhaust piping, and exhaust gas fan is connected with deduster, waste gas One end of pipeline is connected with deduster, and the other end is connected to the top of toroidal cavity, and exhaust piping connects heat exchanger.
The present invention uses the loop configuration being made up of inside and outside ringwall, arranges multilayer lintel, it is simple to gas in kiln body between inside and outside ringwall Being uniformly distributed of stream, it is simple to the uniform calcination of lime stone and multiaspect calcining, it is to avoid sizing phenomenon, have production efficiency high, The features such as energy consumption is low, environmental protection, operation is safe, simple to operate, floor space is little, small investment, the single seat ring-shaped shaft kiln odd-numbered day can Produce lime more than 750 tons.
Accompanying drawing explanation
Fig. 1 is the structural representation of annular lime shaft kiln of the present invention.
Fig. 2 is the sectional view of kiln body in the present invention.
Fig. 3 is that the layout of lintel in the present invention launches schematic diagram.
Fig. 4 is the structural representation of lintel in the present invention.
In figure: 1, outer ring wall, 2, interior ringwall, 3, lintel, 4, burner, 5, hoist engine, 6, truck, 7, feeding leads Rail, 8, feed bin, 9, distributor chute, 10, cloth valve, 11, ash hoist, 12, ash discharge gate valve, 13, middle ash silo, 14, cooling blower, 15, combustion fan, 16, exhaust gas fan, 17, deduster, 18, heat exchanger, 19, combustion tube Road, 20, exhaust piping, 21, chimney, 22, lime stone, 23, space.
Detailed description of the invention
Fig. 1 gives the overall structure of the coal gas calcining annular lime shaft kiln of the present invention, mainly includes kiln body, the cross section of kiln body Structure is as shown in Figure 2.This kiln body is made up of outer ring wall 1 and interior ringwall 2, and interior ringwall 2 is arranged in outer ring wall 1, both Between form toroidal cavity, be provided with connection the outer ring wall 1 and multilayer (2-6 layer) of interior ringwall 2 in toroidal cavity from top to bottom Lintel 3, material (lime stone) falls and resident in the toroidal cavity having lintel.The layout of lintel 3 as it is shown on figure 3, The structure of lintel 3 as shown in Figure 4, is provided with cavity bottom it.The inwall of outer ring wall 1 and the outer wall of interior ringwall 2 are all with resistance to Fire lining.Toroidal cavity is divided into preheating zone, burning zone and cooling zone (to be respectively at the top of toroidal cavity, middle part from top to bottom And bottom), the lower end part that outer ring wall 1 and interior ringwall 2 are in burning zone is equipped with burner 4, and burner 4 is in two rows Burner on interlaced arrangement, outer ring wall 1 and interior ringwall 2 is to spray.Each layer of burner is respectively positioned between two-layer lintel.Burner 3 Air-flow can go directly in the middle of kiln thorax, kiln temperature is evenly distributed, it is to avoid temperature excessively concentrates generation burning.
Lintel 3 is set between outer ring wall 1 and interior ringwall 2, has the effect that
1. lime stone cloth again when lintel 3, it is simple to the uniform calcination of lime stone;
2. lime stone realizes stirring when lintel 3, it is simple to the multiaspect calcining of lime stone;
3. lintel 3 is set and can improve blanking velocity, it is to avoid sizing;
4. the space 23 (seeing Fig. 3) that lintel 3 bottom is formed in lime stone 22 because of angle of repose both can realize kiln temperature Directly measure, be easy to again being uniformly distributed of airstream in kiln.
Additionally, be provided with material-feeding mechanism in the upper end of toroidal cavity, the bottom of toroidal cavity is provided with discharging mechanism, outer ring wall 1 Outside be provided with feed mechanism, combustion-supporting mechanism, cooling body and waste gas dedusting system.
Feed mechanism includes hoist engine 5, truck 6 and loading guide 7, and truck 6 is arranged on loading guide 7, and and elevator Machine 5 connects.Material is contained in truck 6, and under hoist engine 5 drives, truck 6 is up along loading guide 7, moves to Loading guide 7 upper end, is poured into material in feed bin 8.
Material-feeding mechanism includes feed bin 8, distributor chute 9 and cloth valve 10, and feed bin 8 is positioned at the lower section of loading guide 7 upper end, The bottom of feed bin 8 is provided with multiple distributor chute 9, and each distributor chute 9 is equipped with cloth valve 10, and cloth valve 10 is permissible It is various valves electronic, that pneumatically or hydraulically control.Each distributor chute 9 is connected between outer ring wall 1 and interior ringwall 2, And connect with described toroidal cavity.
Discharging mechanism includes discharging machine 11, discharging gate valve 12 and middle ash silo 13, and discharging machine 11 is distributed in the end of toroidal cavity End, and is connected between outer ring wall 1 and interior ringwall 2, and each discharging machine 11 is respectively provided with a discharging gate valve 12, each go out The lower end of material machine 11 is all connected with ash silo 13.The quick lime being stored in ash silo 13 is exported by belt conveyor.
Combustion-supporting mechanism includes that combustion fan 15, heat exchanger 18 and combustion-supporting pipeline 19, combustion fan 15 are handed over heat by pipeline Parallel operation 18 connects, and heat exchanger 18 is connected to the burning zone outside outer ring wall 1 and within interior ringwall 2 by combustion-supporting pipeline 19 Place.The cold air of combustion fan 15 blowout becomes hot blast after over-heat-exchanger 18 exchanges, for providing HTHP in kiln body Combustion air.Heat exchanger 18 is arranged on exhaust piping, can make full use of the waste heat of waste gas, improves the temperature of combustion air, Reduce EGT, energy-conserving and environment-protective;Heat exchanger 18 uses deashing convenient vertical air preheater.
Cooling body includes cooling blower 14 and cooling pipe, and cooling blower 14 is by the cooling of cooling pipe with toroidal cavity Band connects, for providing high pressure cooling wind bottom kiln body.
Waste gas dedusting system includes exhaust gas fan 16, deduster 17 and exhaust piping 20, exhaust gas fan 16 and deduster 17 Connecting, one end of exhaust piping 20 is connected with deduster 17, and the other end is connected to the top of toroidal cavity, exhaust piping 20 Upper connection has heat exchanger 18.Deduster 18 uses sack cleaner.Start exhaust gas fan 16, the high temperature in toroidal cavity Waste gas sucks heat exchanger 18 through exhaust piping 20, the cold air heat exchange being blown into combustion fan 15, enters and remove after cooling Dirt device 17, is discharged by deduster 17 after filtering dust, filters the waste gas after dust and enters air through chimney 19.EGT The service life of deduster 17 can be extended after reduction.
If the internal diameter 5.6 meters of design kiln body, external diameter 9.6 meters, highly 26 meters, production capacity is up to 750 ton day Lime stone lumpiness: 30~60 or 40~80mm, using cold clean producer gas is fuel, energy consumption :≤1100kcal/kg, Activity of lime is 200~280ml, lime waste gas kiln discharge temperature: 350~420 DEG C.

Claims (2)

1. an annular lime shaft kiln, including kiln body, is characterized in that, described kiln body is made up of, in inner ring outer ring wall and interior ringwall Form toroidal cavity between wall and outer ring wall, in toroidal cavity, be provided with connection outer ring wall and the lintel of interior ringwall, toroidal cavity The position being in burning zone on preheating zone, burning zone and cooling zone, outer ring wall and interior ringwall it is divided into be equipped with burner from top to bottom; Described lintel layered arrangement from top to bottom in toroidal cavity;Described burner is two rows interlaced arrangement, outer ring wall and inner ring Burner on wall is to spray, and each layer of burner is respectively positioned under lintel.
Annular lime shaft kiln the most according to claim 1, is characterized in that, the upper end of described toroidal cavity is provided with material distributing machine Structure, the bottom of toroidal cavity is provided with discharging mechanism, and the outside of described outer ring wall is provided with feed mechanism, combustion-supporting mechanism, cooling Mechanism and waste gas dedusting system;Described combustion-supporting mechanism includes that combustion fan, heat exchanger and combustion-supporting pipeline, combustion fan are handed over heat Parallel operation connects, and heat exchanger is connected to outside outer ring wall by combustion-supporting pipeline and at the burning zone in inner ring portion within the walls;Described waste gas Dust pelletizing system includes exhaust gas fan, deduster and exhaust piping, and exhaust gas fan is connected with deduster, one end of exhaust piping with remove Dirt device connects, and the other end is connected to the top of toroidal cavity, and exhaust piping connects described heat exchanger.
CN201510205835.5A 2015-04-27 2015-04-27 annular lime shaft kiln Active CN104803618B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510205835.5A CN104803618B (en) 2015-04-27 2015-04-27 annular lime shaft kiln

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510205835.5A CN104803618B (en) 2015-04-27 2015-04-27 annular lime shaft kiln

Publications (2)

Publication Number Publication Date
CN104803618A CN104803618A (en) 2015-07-29
CN104803618B true CN104803618B (en) 2016-09-07

Family

ID=53688879

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510205835.5A Active CN104803618B (en) 2015-04-27 2015-04-27 annular lime shaft kiln

Country Status (1)

Country Link
CN (1) CN104803618B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105157415B (en) * 2015-09-01 2018-03-09 北京嘉永会通能源科技有限公司 Ring-shaped shaft kiln
CN111006501A (en) * 2019-11-28 2020-04-14 北京科技大学 Inner and outer ring alternating type heating device and method for high-temperature uniform calcination of shaft kiln
CN111099844B (en) * 2020-01-03 2023-06-23 中冶长天国际工程有限责任公司 Multi-row inserting plate type lime shaft kiln material distribution system and material distribution method
CN111559877B (en) * 2020-05-27 2022-02-08 山西中齐锐能高温材料有限公司 Ultrahigh-temperature shaft kiln
CN111732351B (en) * 2020-06-29 2021-08-20 东北大学 Sleeve lime kiln with combustion chambers distributed in staggered height
CN111807727A (en) * 2020-09-02 2020-10-23 山东万方窑炉工程科技有限责任公司 Double-rectangular-chamber heat-accumulation parallel-flow lime shaft kiln

Also Published As

Publication number Publication date
CN104803618A (en) 2015-07-29

Similar Documents

Publication Publication Date Title
CN104803618B (en) annular lime shaft kiln
CN102303956B (en) Sleeve-type lime kiln
CN102219402B (en) Method and device for calcining materials
CN109776002B (en) Suspension calcination activation system and method suitable for clay mine tailings
CN108264248A (en) A kind of light-burned MgO suspension calcinings production technology and device
CN105731838B (en) A kind of calciner and method that light calcined magnesia is prepared with giobertite
CN102992661B (en) Beam type heat storage lime kiln
CN102230726B (en) Sleeve type continuous calcining vertical kiln
CN106495508A (en) A kind of environmental protection and energy saving light calcined magnesia calcining kiln
CN201242342Y (en) Shaft kiln
CN108164161A (en) A kind of extra light calcined magnesia suspended state calcination system and preparation method of magnesia
CN208218696U (en) A kind of light-burned MgO suspension calcining process units
CN204550403U (en) Annular lime shaft kiln
CN116659249A (en) External channel supporting type double-chamber lime kiln for mixing and blowing and production method
CN207998558U (en) A kind of extra light calcined magnesia suspended state calcination system
CN105157415B (en) Ring-shaped shaft kiln
CN103482889B (en) Heat accumulating type material calcinating device
CN204923825U (en) Alumina shaft kiln is calcined to flaring formula circular section
CN206891148U (en) A kind of bicyclic room alternately heating filters dirt intellectuality calciner plant certainly
CN102557491A (en) Compound combustion beam for lime kiln
CN202193734U (en) Sleeve type lime kiln
CN102183142B (en) Semi-heat accumulating type rotating bed equipment and process for producing large-size high-activity lime
CN2666909Y (en) Energy-saving environment protection active lime burning-in shaft kiln
CN105565687B (en) A kind of limekiln breeze blowing induction system
CN108518685A (en) A kind of circulating fluidized bed boiler

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant