CN108955276A - Vertical sinter cooler and sinter cooling means with revolving top - Google Patents

Vertical sinter cooler and sinter cooling means with revolving top Download PDF

Info

Publication number
CN108955276A
CN108955276A CN201710367694.6A CN201710367694A CN108955276A CN 108955276 A CN108955276 A CN 108955276A CN 201710367694 A CN201710367694 A CN 201710367694A CN 108955276 A CN108955276 A CN 108955276A
Authority
CN
China
Prior art keywords
discharge
cooling
chute
vertical
sinter
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.)
Granted
Application number
CN201710367694.6A
Other languages
Chinese (zh)
Other versions
CN108955276B (en
Inventor
张震
贺新华
刘克俭
孙英
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.)
Zhongye Changtian International Engineering Co Ltd
Original Assignee
Zhongye Changtian International Engineering 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 Zhongye Changtian International Engineering Co Ltd filed Critical Zhongye Changtian International Engineering Co Ltd
Priority to CN201710367694.6A priority Critical patent/CN108955276B/en
Publication of CN108955276A publication Critical patent/CN108955276A/en
Application granted granted Critical
Publication of CN108955276B publication Critical patent/CN108955276B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D15/00Handling or treating discharged material; Supports or receiving chambers therefor
    • F27D15/02Cooling
    • F27D15/0286Cooling in a vertical, e.g. annular, shaft
    • 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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

Vertical cooling machine with revolving top, comprising: revolving top (1), umbrella chute (2), vertical chute (3), the tower body, cooling section (6) and the tower body that are made of tower body top cover (4) and tower body side wall (5) top cover or side wall upper part setting hot-blast outlet (10);Wherein: umbrella chute (2) includes the overall section (201) on top and the separated section (202) of lower part, the upper end of overall section (201) is connect with revolving top (1), each branch vertical chute (3) connection corresponding with lower section of section (202) is separated, the gas compartment between the top of cooling section (6), vertical chute (3) and tower body forms hot-air channel (7);The lower section of cooling section (6) is equipped with uniform air intake device (8);Lower section of multiple discharge cone bucket (9) settings in uniform air intake device (8);Discharge apparatus is equipped with the lower section of discharge cone bucket (9).The configuration of the present invention is simple, sealed reliable, waste heat recovery efficiency are high.

Description

Vertical sinter cooler and sinter cooling means with revolving top
Technical field
The present invention relates to sinter cooler and sinter cooling means with revolving top, belong to ironmaking field and Environment protection field.
Background technique
During modern sintering process, " cooling " is more crucial one of process.Sinter is in the roasting by sintering machine After burning, high temperature finished product mine has been formed, it is how cooling to its progress protectiveness under the premise of not influencing its quality and yield rate, It can be sent into finished product ore storage bin through belt feeder, while the sensible heat energy perfection entrained by it being recycled, be all the time The problem of skilled worker constantly studies in the industry.Since the 1960s, the cooling technique of sinter is rapidly developed, It is broadly divided into cooling belt, ring type cooling and the cooling three categories of disc type.In the market competition in later period, belt cooling technology is washed in a pan It eliminates, remaining ring type is cooling respectively to have its advantage and disadvantage with disc type cooling technology.But it is comprehensively compared, the cold UTILIZATION OF VESIDUAL HEAT IN colder than ring of disk Rate is more preferable (all sintering mine sensible heats are recycled), therefore disk cold is very widely used in overseas market, and this patent is also It is illustrated around disk cold technology.
Disk cold technology develops since the seventies, most starts cold for transverse type disk, i.e., cooling wind is out of disk cold Circumferential outer ring flowing, is horizontally through the bed of material to be cooled and exchanges heat with it, and the cooling wind after having exchanged heat is directly outer to drain into atmosphere.It does so Both uneconomical or not environmentally, optimize by continuous research for many years, newest disk cold technology is Mitsubishi Hitachi in It contains " air-draft-type longitudinal direction disk refrigeration technique " that steel proposes.This technology uses exhausting, and cooling wind is pumped into material bottom to be cooled from atmosphere Portion, then up longitudinally through the bed of material, finally from bed of material top, blowout enters subsequent handling.The program and the scheme phase most started Than having had very big optimization and progress, having described in detail below for the program.
JP2008232519A (Hitachi of Mitsubishi and middle Sheng steel, call D1 in the following text) discloses air-draft-type longitudinal direction disk refrigeration technique, referring to Fig. 1 therein: heat sinter enters feed chute from sintering machine tail clan, the stock column of certain altitude is piled into chute, in this way On the one hand it is to play the role of uniform blanking, is on the other hand to play material envelope to prevent feed inlet string wind action.Mineral aggregate continue to It is lower to enter in disk cold cabinet after hood, push the stock column at certain altitude.At the same time, by the negative pressure shadow of exhaust fan It rings, the air near disk cold can be inhaled into stock column via blinds air-intake device, passed through stock column from the bottom up and exchanged heat therewith, change Air after heat is pierced by from stock column top surface into air outlet, is sent to gravitational precipitator and waste heat boiler, finally by taking out By outlet after blower.Being formed cross section at disk cold lower tray by air sintering feed after cooling is 37 degree of stocking angle triangles The annular accumulation area of shape, when being turned to discharge zone, sintering feed is scraped by scraper plate device, and completion cooling process enters next A process links.
Hitachi of Mitsubishi and it is middle contain steel " air-draft-type longitudinal direction disk refrigeration technique " although having marked improvement compared with routine techniques, but still So there is following five point defect:
1) device whole height requires excessively high: since " air-draft-type longitudinal direction disk refrigeration technique " takes exhausting mode, so necessary Material envelope, that is, the stock column accumulated in feed chute in Fig. 1 of D1 are set in gating location, material envelope height is with disk cold case 1.2~1.5 times of internal stock column height are standard.The height of whole series of discs device for cooling is thus virtually increased, is pacified in construction When dress or just needs to rise whole sintering machine absolute altitude or just need down to dig the civil engineering plane of disk cold.Regardless of choosing Which kind of mode is selected, a high cost of investment can be all caused, it is very not cost-effective in economic indicator;
2) distinguished and admirable open circuit circulation causes utilization rate of waste heat low and pollutes environment: due to the wind of " air-draft-type longitudinal direction disk refrigeration technique " Stream is open circuit circulation, and the direct outlet of air come out from waste heat boiler does not recycle, and causes also more than 100 degree in this way Air sensible is wasted, and contains a large amount of little particle dust in the air of outlet, causes a degree of particle for atmosphere Object pollution;
3) material serious wear at feed inlet: since " air-draft-type longitudinal direction disk refrigeration technique " setting material seals at feed chute, Therefore one section of frictional distance is had between charge level upper layer in material envelope lower part and disk cold cabinet.Sintering feed is expected in high temperature and top at this time Under the double-deck bad working environments that column squeezes, it is easy to dusting when being rubbed and becomes broken, to reduce the yield rate of sintering machine;
4) environmental pollution is more serious: the negative pressure exhausting technology taken due to " air-draft-type longitudinal direction disk refrigeration technique ", thus it Not set sealing closure assembly at lower box pallet.In this way when sinter is scraped by scraper device, it be easy to cause a large amount of subtle Particle and dust splash.And once exhaust fan breaks down maintenance, the material dust pushed around disk cold can all enter big Gas, causes the operating environment by machine and its bad influence.
5) the waste heat boiler thermal efficiency is not up to highest: since " air-draft-type longitudinal direction disk refrigeration technique " be not the air for being pierced by the bed of material It is precisely classified according to wind-warm syndrome, but is all mixed into waste heat boiler, it, will certainly in this way when low-temperature zone outlet wind-warm syndrome is too low The air themperature into waste heat boiler is dragged down, to reduce the thermal efficiency value of waste heat boiler.
Currently, sinter is cooling mainly using the conventional belt based on strong wind rapid cooling, disposable handling cooling principle Cooler or circular cooler.Regardless of using which kind of type of cooling, it is big all to there is air leak rate of air curtain in cooler, and blower power consumption is high, sensible heat The problems such as rate of recovery is low, and boiler thermal efficiency is low.In other words, in the Vehicles Collected from Market requirement with green manufacturing energy-saving to sintering production Under the overall situation being increasingly stringenter, originally device structure has been difficult to realize sintering mine sensible heat high efficiente callback and has utilized.
Therefore, the limitation that traditional ring type is cooling or belt is cooling is broken through, a kind of sintering mine sensible heat high efficiente callback is developed Technique and technical equipment have been the energy-saving and environment-friendly only ways of sintering industry.
Summary of the invention
Therefore, by proposing a kind of based on small wind to a large amount of research work of domestic and international sintering mine sensible heat recycling aspect Slow cooling sinter adverse current deep bed sintering cooling technique.The technique has sinter cooling velocity slow, and ton consumption cooling air quantity is small, exhausted air quantity Relatively small, exhaust gas temperature is high, and boiler thermal efficiency is high, and cooling exhaust gas can all be utilized by boiler, the sintering mine sensible heat rate of recovery one As up to 70% or so cooling feature.According to sinter adverse current deep bed sintering cooling technique, a kind of vertical cooling machine has been invented, it should Vertical cooling machine has cloth uniform, and discharge is uniform, the uniform feature of cloth wind, therefore the cooler good cooling results, hot blast temperature Height meets the requirement of sinter adverse current deep bed sintering cooling technique.
The invention vertical cooling machine compared with former ring cold machine, do not leak out by simple structure and reliable sealing, plant maintenance amount Small, waste heat recovery efficiency is high.
According to the invention ,the aim of the invention is to provide a kind of vertical cooling machine for cooling down sinter, it is tower structure, because This, also referred to as tower cooler.
According to the present invention, a kind of vertical cooling machine with revolving top is provided, which includes: rotation cloth Device, umbrella chute, vertical chute, the tower body, cooling section and the tower body that are made of tower body top cover and tower body side wall top cover or side wall The hot-blast outlet of top setting;Wherein: umbrella chute includes the overall section on top and the separated section with multiple branches of lower part, The upper end of overall section is connect with revolving top, separates each branch vertical chute connection corresponding with lower section of section, The top of tower body side wall is arranged in tower body top cover, and vertical chute is arranged on tower body top cover, and the lower end of vertical chute is protruded into In tower body, the branches end for separating section of the upper end and umbrella chute connect, the top of umbrella chute is arranged in revolving top, The lower part of tower body is arranged in cooling section;
The gas compartment (no material space) between the top of cooling section, vertical chute and tower body forms hot-air channel;
The lower section of cooling section is equipped with uniform air intake device;
The lower section of uniform air intake device is arranged in multiple discharge cone buckets;With
The lower section of discharge cone bucket is equipped with discharge apparatus.
Preferably, in tower body, the front end of hot-blast outlet be equipped with radiation heat regenerator.Preferably, recuperation of heat is radiated Device uses fin type heat exchanger or tubulation type heat exchanger.
Preferably, discharge apparatus is oscillating feeder or plate belt feeder.
Preferably, the lower section of oscillating feeder end is equipped with cold sinter conveying device.
Preferably, discharge apparatus is plate belt feeder, and discharge chute is equipped with below the discharge port of plate belt feeder or is unloaded The lower section of hopper, discharge chute or dump skip is equipped with cold sinter conveying device.
It is preferred that the end of discharge cone bucket is equipped with gate valve.
It is preferred that the lower part (preferably along circumferencial direction) of cooling section is equipped with temperature probe;Preferably, the temperature probe For thermocouple temperature sensor.
It is preferred that uniform air intake device includes outer ring blast pipe, multiple air duct branch pipes and the inner ring air inlet of annular or " C " shape Road, in which: the outer periphery of tower wall is arranged in the outer ring blast pipe of annular or " C " shape, and inner ring air inlet duct is arranged in tower body bottom, One end connection outer ring blast pipe of each air duct branch pipe connects inner ring air inlet duct with the other end.Preferably, inner ring air inlet duct Side wall or side be shutter.
It is preferred that the quantity of the branch of the separated section of umbrella chute and the quantity of corresponding vertical chute are 3-12, it is excellent It is selected as 4-10, more preferably 6-8.
It is preferred that multiple discharge cone buckets are presented annular spread in uniform air intake device lower end or circumferentially equably divide Cloth.
Generally, the number of discharge cone bucket is 4-12, preferably 6-10,6-8.
Generally, the quantity of air duct branch pipe is at least one in uniform air intake device, preferably 2-12, preferably 3-10, more It is preferred that 4-8, more preferable 6-8.
It is preferred that the top of inner ring air inlet duct is sealing and lower end is opening.
Generally, uniform air intake device includes 1 or 2 inner ring air inlet duct;Preferably, when there is 2 inner ring air inlet ducts, it Upper and lower setting each other.
It is preferred that discharge apparatus is the double-deck oscillating feeder;The double-deck oscillating feeder include body rack, upper layer vibra shoot, Lower layer's vibra shoot, vibrator;Upper layer vibra shoot and lower layer's vibra shoot are arranged on body rack, and upper layer vibra shoot is located at lower layer's vibration The top of dynamic slot, upper layer vibra shoot and lower layer's vibra shoot are connect with vibrator respectively.Preferably, upper layer vibra shoot and/or under Layer vibra shoot is equipped with regulating device, and regulating device adjusts the bottom plate inclination angle of lower layer's vibra shoot.
It is preferred that vibrator includes upper layer vibrator and lower layer's vibrator, upper layer vibrator is connect with upper layer vibra shoot, lower layer Vibrator is connect with lower layer's vibra shoot.Preferably, upper layer vibra shoot and lower layer's vibra shoot are arranged by spring in body rack On.
It is preferred that the vertical cooling machine further includes control system, control system and uniform air intake device, cold sinter conveying are filled It sets, the connection of gate valve, temperature probe, discharge apparatus, and controls uniform air intake device, cold sinter conveying device, gate valve, survey The operation of temperature probe, discharge apparatus.
According to the present invention, a kind of sinter cooling means or next cold using a kind of above-described vertical cooling machine is also provided But the method for sinter, method includes the following steps:
(1) sinter enters in the revolving top of vertical cooling machine, under gravity continuous flowing from top to bottom, Enter vertical chute via umbrella chute, is then deposited in the tower body of cooler;
(2) uniform air intake device conveying cooling gas (such as air) of vertical cooling machine enters tower by inner ring air inlet duct In vivo, cooling gas passes through from bottom to top is deposited in the intracorporal sinter bed of material of tower, and carries out countercurrent heat exchange, heat with sinter Cooling gas temperature gradually rises after exchange, and sinter charge level is discharged in vertical cooling machine tower, forms high-temperature hot-air, high warm Wind is discharged through hot-air channel from hot-blast outlet;Preferably, high-temperature hot-air is transported to afterheat utilizing system (such as cogeneration System) in;
(3) be deposited in the intracorporal sinter of tower of cooler and cooling gas from bottom to top carry out countercurrent heat exchange and by It is cooling, it enters in the discharge cone bucket of vertical cooling machine lower part, is then discharged by oscillating feeder or is passed through by plate belt feeder Discharge chute or dump skip are discharged in cold sinter conveying device;With
(4) radiant heat energy of radiation heat regenerator recycling sinter generates high-temperature vapor, and vapor passes through recovery tubes Road enters in afterheat generating system.
It is preferred that control system controls uniform air intake device, cold sinter conveying dress according to temperature probe temperature detected It sets, the operation of gate valve, temperature probe, discharge apparatus.
It is preferred that with each, discharge cone bucket is corresponding that temperature probe is arranged above it, according to each temperature probe institute The temperature of detection, control system control the operation of corresponding discharge apparatus.
The equipment also has self feed back discharge regulatory function.The sinter temperature of corresponding region is detected by temperature probe, After the sinter temperature of some circumferential position of detection reaches cooling effect, the corresponding discharge cone in the region is just normally opened Discharge apparatus below struggling against, carries out normal discharge, sets conversely, then accordingly decreasing the discharge velocity of discharge apparatus or closing discharge It is standby, it allows the sinter in the region to cool down a period of time again, after sinter temperature reaches cooling effect, then carries out normal discharge. It is also possible to carry out the adjusting of discharge velocity by the insertion depth for adjusting gate valve.
In the present invention, it is however generally that, the vertical cooling machine is mainly by revolving top, umbrella chute, vertical chute, tower Body, uniform air intake device, cooling section, discharge cone bucket, discharge apparatus, hot-blast outlet composition.
Revolving top is located at the top of vertical cooling machine, can enter along tower body central axis rotary motion, heat sinter After revolving top, flowed out under the effect of gravity from revolving top chute, into umbrella chute, during charging, Revolving top rotary motion enables material to be evenly distributed on umbrella chute.
Umbrella chute is a umbrella shape chute, and upper end is disposed with revolving top, and lower end connects vertical chute, umbrella chute point For upper and lower two parts, overall section and separated section.Overall section is integral umbrella chute, separates section and is located at below overall section, is One circumferentially equally distributed several segments umbrella chute separates and keeps apart between the chute of section.It is planted from revolving top Sinter is evenly distributed on umbrella chute, continues to flow downwardly through overall section and separated section, enters slipping vertically for lower section Slot.
For one, circumferentially several equally distributed Vertical Channels, each channel correspond umbrella chute point to vertical chute Open the umbrella chute of section, vertical chute is divide into upper part and lower part by vertical cooling machine top cover, wherein the intracorporal vertical chute of tower it Between form hot-air channel, the hot wind between vertical chute can be flowed out on the outside of vertical chute from hot-air channel between tower body Hot-blast outlet discharge is flowed into without material space, then from no material space.The sinter flowed out from umbrella chute is flowed into vertical chute It is interior, then flowed downward out from vertical chute, it enters in cooling section, forms uniform annular material heap in cooling section.
Cooling section is mainly a shell structure, cooling section is entered by the sinter that vertical chute flows down, in cooling In section, the cooling wind blown up from uniform air intake device carries out heat exchange with sinter in cooling section, and sinter is cooling, changes Cooling wind after heat becomes hot wind, and hot wind can be discharged from the free charge level on cooling section top, enters no material space.After cooling Sinter enter the uniform air intake device of cooling section lower end, flowed out from the material channel of uniform air intake device.
Uniform air intake device is mainly made of outer ring blast pipe, inner ring air inlet duct, multiple air duct branch pipes, major function be by Cooling wind is blown into the cooling section above it, cools down to sinter.Wherein, outer ring blast pipe is a circulating line, air blast The pressure cooling wind that machine conveying comes enters outer ring blast pipe, and cooling wind is equably conveyed to air duct branch by outer ring blast pipe Pipe;Inner ring air inlet duct be a circulating line, inner ring air inlet duct both side plate be venetian blind type structure, inner ring air inlet duct top seal, Cooling wind is introduced into inner ring air inlet duct by lower ending opening by air duct branch pipe from outer ring blast pipe, cold in inner ring air inlet duct But wind can be equably upwardly into the sinter in cooling section from inner ring air inlet duct two sides shutter, to sinter It is cooled down.Wherein outer ring blast pipe, inner ring air inlet duct, constitute material channel between the branch pipe of air duct, what cooling section flow down Sinter can flow downwardly into discharge cone bucket by material channel.
Discharge cone bucket is located at uniform discharge air blast section lower end, it is evenly distributed in the circumferential direction several, generally 4-8, Its shape is up big and down small abnormity or circle or pyramidal structure.Sinter after cooling by gravity flows into discharge cone In bucket.Each discharge cone bucket lower end connects a discharge apparatus, can control the discharge of each discharge cone bucket by discharge apparatus Speed.
In the present invention, discharge apparatus be oscillating feeder or plate belt feeder, using oscillating feeder or it is board-like give mine Machine carries out discharge, has discharge uniform, and Maintenance and Repair are convenient, the small advantage of maintenance workload.
Hot-blast outlet is located on vertical cooling machine top tower body side wall, is connected to no material space inside, in no material space Hot wind is discharged by hot-blast outlet, into subsequent afterheat generating system.
Preferably, gate valve is arranged in discharge cone bucket lower end, can end material after gate valve is inserted into discharge cone bucket, no It flows downward.During normal production, gate valve is opened, and when the corresponding discharge apparatus below discharge cone bucket needs to overhaul, will be inserted Plate valve is inserted into discharge cone bucket, is ended material, is overhauled.
By the broken heat sinter of single roll crusher, vertical cooling machine top is transported by heat sinter conveying device Portion, through the revolving top at the top of it, equably cloth flows into the vertical chute of lower section on umbrella chute by umbrella chute, Continuous flowing from top to bottom by vertical chute flows into the cooling section of lower section to sinter under the effect of gravity, in cooling section with Cooling wind carries out countercurrent heat exchange and flows downward after sinter is cooled to 150 DEG C or less, flows through the object of uniform air intake device Expect channel, enter in the discharge cone bucket of lower section, then cold sinter conveying dress is discharged to by the discharge apparatus of discharge cone bucket lower end It sets, then sinter after cooling is transported into subsequent processing by cold sinter conveyer.
Cooling gas passes through confession under the action of air blower, from the inner ring air inlet duct of uniform air intake device with certain pressure Enter in cooling section, passes through the sinter bed of material of cooling section from bottom to top, and carry out countercurrent heat exchange with sinter.It is cold after heat exchange But gas temperature gradually rises, and is discharged through the free charge level of cooling section, forms high-temperature hot-air.High-temperature hot-air is through vertical cooling machine top Without material space, be discharged by hot-blast outlet, the high-temperature hot-air of discharge enters subsequent afterheat generating system.
The surface toughness of the pelletizing shape sinter of high temperature, once it is cooling, it is adhered to one another, the equipment of the prior art Discharge difficulty is often resulted in, still, equipment of the invention has well solved this problem.
Generally, the height of tower body is usually 4-24 meters, and preferably 4.5-22 meters, preferably 5-18 meters, preferably 6-12 meters, more preferably 7-10 meters.The overall diameter of tower body is generally 8-30 meters, and preferably 9-27 meters, preferably 10-25 meters, preferably 11-22 meters, more preferable 12- 20 meters.
Compared with prior art, the present invention has following advantageous effects:
Cloth is uniform in present device, and discharge is uniform, and cloth wind is uniform.Also region discharge tune can be carried out according to cooling effect Function is saved, therefore the cooler good cooling results, hot blast temperature height meet the requirement of sinter adverse current deep bed sintering cooling technique.
The invention vertical cooling machine compared with the ring cold machine of the prior art, do not leak out by simple structure and reliable sealing, if Standby maintenance is small, and waste heat recovery efficiency is high.Cooling feature of the sintering mine sensible heat rate of recovery generally up to 71% or so.
The technique can also overcome the problems, such as double sintering of the sinter in vertical cooling device, prevent vertical cooling device There is blocking phenomenon.
1, structure is simple, reduces equipment investment, and reduce the operating cost of equipment;
2, the heat recovery efficiency of the good airproof performance of device, sinter is high and obtains the exhaust gas (hot wind) of high temperature for producing Raw steam, and for generating electricity in the form of high-temperature steam, electricity generation efficiency is higher;
3, discharge significantly reduces the frequency shut down, overhauled without clogging;
It 4, can be by independently controlling each discharge according to the temperature of the top material of each discharge cone bucket detected The discharge velocity of cone bucket, to adjust the temperature;
5, sinter radiates heat recovery function: the heat sinter temperature for having just enter into tower body is very high, by bed of material surface to tower Internal radiation thermal energy, is set in tower body, the radiation heat regenerator of hot-blast outlet front end can recycle radiant heat energy, is converted to height Warm steam enters afterheat generating system by recuperation of heat pipeline.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of the vertical cooling machine with revolving top of the present invention;
Fig. 2 is the cross-sectional view of the position A-A in Fig. 1;
Fig. 3 is the cross-sectional view of the position B-B in Fig. 1;
Fig. 4 is the cross-sectional view of the position C-C in Fig. 1;
Fig. 5 is discharge cone bucket layout drawing of the present invention;
Fig. 6 is uniform air intake apparatus structure schematic diagram of the present invention;
Fig. 7 is the structural schematic diagram of umbrella chute of the present invention;
Fig. 8 is the structural scheme of mechanism of vibrator there are two the double-deck oscillating feeder of the present invention is set;
Fig. 9 is the structural scheme of mechanism that the double-deck oscillating feeder of the present invention is equipped with a vibrator;
Figure 10 is the structural schematic diagram of another vertical cooling machine with revolving top of the present invention;
Figure 11 is the structural schematic diagram of the third vertical cooling machine with revolving top of the invention;
Figure 12 is the schematic diagram of the radiation heat regenerator of pipe type;
Figure 13 is plate belt feeder schematic layout pattern of the present invention;
Figure 14 is a kind of control system schematic diagram of vertical cooling machine of the present invention.
Appended drawing reference: 1: revolving top;2: umbrella chute;201: umbrella chute overall section;202: umbrella chute separates Section;3: vertical chute;4: tower body top cover;5: tower body side wall;6: cooling section;7: hot-air channel;8: uniform air intake device;801: outer Ring blast pipe;802: air duct branch pipe;803: inner ring air inlet duct;804: blast main;9: discharge cone bucket;10: hot-blast outlet;11: cold Sinter conveying device;12: gate valve;13: temperature probe;14: plate belt feeder;15: discharge chute or dump skip;P: vibration Batcher;P01: body rack;P02: upper layer vibra shoot;P03: lower layer's vibra shoot;P04: vibrator;P0401: upper layer vibration Device;P0402: lower layer's vibrator;P05: regulating device;F01: radiation heat regenerator;F0101: the water inlet of heat regenerator is radiated; F0102: the steam (vapor) outlet of heat regenerator is radiated;F02: recuperation of heat pipeline (jet chimney);K: control system.
Specific embodiment
As shown in Fig. 1-13, according to the present invention, a kind of vertical cooling machine with revolving top, the cooler are provided It include: revolving top 1, umbrella chute 2, vertical chute 3, tower body, the cooling section 6 being made of tower body top cover 4 and tower body side wall 5 And the hot-blast outlet 10 of top cover or the side wall upper part setting of tower body;Wherein: umbrella chute 2 includes the overall section 201 on top under The separated section 202 with multiple branches in portion, the upper end of overall section 201 are connect with revolving top 1, separate each of section 202 A branch vertical chute 3 corresponding with lower section connects, and the top of tower body side wall 5, vertical chute 3 is arranged in tower body top cover 4 It is arranged on tower body top cover 4, and the lower end of vertical chute 3 is protruded into tower body, the upper end with umbrella chute 2 separates section 202 Branches end connection, the top of umbrella chute 2 is arranged in revolving top 1, and the lower part of tower body is arranged in cooling section 6;
The gas compartment (no material space) between the top of cooling section 6, vertical chute 3 and tower body forms hot-air channel 7;
The lower section of cooling section 6 is equipped with uniform air intake device 8;
The lower section of uniform air intake device 8 is arranged in multiple discharge cone buckets 9;With
The lower section of discharge cone bucket 9 is equipped with discharge apparatus.
Preferably, in tower body, the front end of hot-blast outlet 10 be equipped with radiation heat regenerator F01.
Preferably, radiation heat regenerator F01 uses fin type heat exchanger or tubulation type heat exchanger.
F0101 is the water inlet for radiating heat regenerator F01, and F0102 is the steam (vapor) outlet for radiating heat regenerator F01.
Preferably, discharge apparatus is oscillating feeder P or plate belt feeder 14.
Preferably, the lower section of the end oscillating feeder P is equipped with cold sinter conveying device 11.
Preferably, discharge apparatus is plate belt feeder 14, is equipped with discharge chute below the discharge port of plate belt feeder 14 Or dump skip 15, the lower section of discharge chute or dump skip 15 are equipped with cold sinter conveying device 11.
It is preferred that the end of discharge cone bucket 9 is equipped with gate valve 12.
It is preferred that the lower part (preferably along circumferencial direction) of cooling section 6 is equipped with temperature probe 13;Preferably, the thermometric Probe 13 is thermocouple temperature sensor.
It is preferred that uniform air intake device 8 includes annular or the outer ring blast pipe 801 of " C " shape, multiple air duct branch pipes 802 and interior Ring air inlet duct 803, in which: the outer periphery of tower wall 5, inner ring air inlet duct is arranged in the outer ring blast pipe 801 of annular or " C " shape 803 settings in tower body bottom, one end connection outer ring blast pipe 801 of each air duct branch pipe 802 connected with the other end inner ring into Air duct 803.Preferably, the side wall of inner ring air inlet duct 803 or side are shutter.
804 be blast main, and the conveying of uniform air intake device 8 cooling gas (such as air) is entered outer by blast main 804 Ring blast pipe 801.
It is preferred that the quantity of the branch of the separated section 202 of umbrella chute 2 and the quantity of corresponding vertical chute 3 are 3-12 It is a, preferably 4-10, more preferably 6-8.
It is preferred that annular spread or circumferentially equably is presented in 8 lower end of uniform air intake device in multiple discharge cone buckets 9 Distribution.
Generally, the number of discharge cone bucket 9 is 4-12, preferably 6-10,6-8.
Generally, the quantity 2-12 of air duct branch pipe 802 is a in uniform air intake device 8, and preferably 3-10, more preferable 4-8, more It is preferred that 6-8.
It is preferred that the top of inner ring air inlet duct 803 is sealing and lower end is opening.
Generally, uniform air intake device 8 includes 1 or 2 inner ring air inlet duct 803;Preferably, when there is 2 inner ring air inlet ducts When 803, their upper and lower settings each other.
It is preferred that discharge apparatus is the double-deck oscillating feeder P;The double-deck oscillating feeder P includes body rack P01, upper layer vibration Dynamic slot P02, lower layer vibra shoot P03, vibrator P04;Upper layer vibra shoot P02 and lower layer vibra shoot P03 is arranged in body rack P01 On, upper layer vibra shoot P02 is located at the top of lower layer vibra shoot P03, upper layer vibra shoot P02 and lower layer vibra shoot P03 respectively with vibration Dynamic device P04 connection.Preferably, upper layer vibra shoot P02 and/or lower layer vibra shoot P03 is equipped with regulating device P05, adjusts dress Set the bottom plate inclination angle that P05 adjusts lower layer's vibra shoot P03.
It is preferred that vibrator P04 includes upper layer vibrator P0401 and lower layer vibrator P0402, upper layer vibrator P0401 with Upper layer vibra shoot P02 connection, lower layer vibrator P0402 are connect with lower layer vibra shoot P03.Preferably, upper layer vibra shoot P02 and Lower layer vibra shoot P03 is arranged on body rack P01 by spring.
It is preferred that the vertical cooling machine further includes control system K, control system K and uniform air intake device 8, cold sinter are defeated Device 11, gate valve 12, temperature probe 13, discharge apparatus connection are sent, and controls uniform air intake device 8, cold sinter conveying dress Set the operation of 11, gate valve 12, temperature probe 13, discharge apparatus.
According to the present invention, a kind of sinter cooling means or next cold using a kind of above-described vertical cooling machine is also provided But the method for sinter, method includes the following steps:
(1) sinter enters in the revolving top 1 of vertical cooling machine, under gravity continuous flow from top to bottom It is dynamic, enter vertical chute 3 via umbrella chute 2, is then deposited in the tower body of cooler;
(2) vertical cooling machine uniform air intake device 8 convey cooling gas (such as air) by inner ring air inlet duct 803 into Enter in tower body, cooling gas passes through from bottom to top is deposited in the intracorporal sinter bed of material of tower, and carries out refluent heat friendship with sinter It changes, cooling gas temperature gradually rises after heat exchange, and sinter charge level is discharged in vertical cooling machine tower, high-temperature hot-air is formed, High-temperature hot-air is discharged through hot-air channel 7 from hot-blast outlet 10;Preferably, high-temperature hot-air is transported to afterheat utilizing system (example Such as afterheat generating system) in;
(3) be deposited in the intracorporal sinter of tower of cooler and cooling gas from bottom to top carry out countercurrent heat exchange and by It is cooling, it enters in the discharge cone bucket 9 of vertical cooling machine lower part, is then discharged by oscillating feeder P or by plate belt feeder 14 It is discharged in cold sinter conveying device 11 by discharge chute or dump skip 15;With
(4) radiant heat energy of radiation heat regenerator F01 recycling sinter generates high-temperature vapor, and vapor passes through recuperation of heat Pipeline F02 enters in afterheat generating system.
It is preferred that it is defeated that control system K controls uniform air intake device 8, cold sinter according to the temperature detected of temperature probe 13 Send the operation of device 11, gate valve 12, temperature probe 13, discharge apparatus.
It is preferred that corresponding with each discharge cone bucket 9 be arranged temperature probe 13 above it, according to each temperature probe 13 temperature detected, control system K control the operation of corresponding discharge apparatus.
The equipment also has self feed back discharge regulatory function.The sinter temperature of corresponding region is detected by temperature probe 13 Degree just normally opens the corresponding row in the region after sinter temperature of some circumferential position of detection reaches cooling effect The discharge apparatus for expecting 9 lower section of cone bucket, carries out normal discharge, conversely, then accordingly decreasing discharge velocity or the closing of discharge apparatus Discharge apparatus allows the sinter in the region to cool down a period of time again, after sinter temperature reaches cooling effect, then carries out normal Discharge.It is also possible to carry out the adjusting of discharge velocity by the insertion depth for adjusting gate valve 12.
Embodiment 1
The height of tower body is 8 meters, and the overall diameter of tower body is 13 meters.The height of discharge cone bucket 9 is 7 meters.Discharge apparatus is vibration Dynamic batcher P.In tower body, the front end of hot-blast outlet 10 be equipped with radiation heat regenerator F01;Using tubulation type heat exchanger, such as scheme Shown in 12.
The daily handling ability of sinter is 8650 ton/days.The temperature of sinter into before in revolving top 1 is 700 DEG C or so, the hot blast temperature of hot-blast outlet 10 reaches 502 DEG C or so.For the heat of recycling for generating electricity, generated energy is about 36 Degree electricity.
Compared with the ring cold machine of the prior art, advantage is: generated energy is high, air leak rate of air curtain is low, dust emission is small, and equipment simply may be used It leans on, due to better tightness, technology of the invention is capable of providing the hot wind of higher temperature for generating high-temperature steam, significantly improves Electricity generation efficiency.
The technique can also overcome the problems, such as double sintering of the sinter in vertical cooling device, prevent vertical cooling device There is blocking phenomenon.Device is run 6 months, putty, stuck problem does not occur.
Embodiment 2
Embodiment 1 is repeated, only discharge apparatus is plate belt feeder 14, as shown in figure 11.

Claims (12)

1.一种具有旋转布料器的立式冷却机,该冷却机包括:旋转布料器(1)、伞状溜槽(2)、竖直溜槽(3)、由塔体顶盖(4)和塔体侧壁(5)构成的塔体、冷却段(6)及塔体的顶盖或侧壁上部设置的热风出口(10);其中:伞状溜槽(2)包括上部的整体段(201)和下部的具有多个分支的分开段(202),整体段(201)的上端与旋转布料器(1)连接,分开段(202)的每一个分支与下方对应的一个竖直溜槽(3)连接,塔体顶盖(4)设置在塔体侧壁(5)的顶部,竖直溜槽(3)设置在塔体顶盖(4)上,并且竖直溜槽(3)的下端伸入塔体内、其上端与伞状溜槽(2)的分开段(202)的分支末端连接,旋转布料器(1)设置在伞状溜槽(2)的顶端,冷却段(6)设置在塔体的下部;1. A vertical cooler with a rotary distributor, the cooler comprises: a rotary distributor (1), an umbrella chute (2), a vertical chute (3), a tower top cover (4) and a tower The tower body formed by the body side wall (5), the cooling section (6) and the top cover of the tower body or the hot air outlet (10) arranged on the upper part of the side wall; wherein: the umbrella-shaped chute (2) includes the upper integral section (201) And the lower split section (202) with a plurality of branches, the upper end of the integral section (201) is connected with the rotary distributor (1), and each branch of the split section (202) corresponds to a vertical chute (3) below connection, the tower body top cover (4) is set on the top of the tower body side wall (5), the vertical chute (3) is set on the tower body top cover (4), and the lower end of the vertical chute (3) extends into the tower In the body, its upper end is connected with the branch end of the split section (202) of the umbrella chute (2), the rotary distributor (1) is arranged at the top of the umbrella chute (2), and the cooling section (6) is arranged at the lower part of the tower body ; 冷却段(6)的上方、竖直溜槽(3)和塔体之间的气体空间(无料空间)形成热风通道(7);Above the cooling section (6), the gas space (material-free space) between the vertical chute (3) and the tower body forms a hot air passage (7); 冷却段(6)的下方设有均匀进风装置(8);A uniform air intake device (8) is provided below the cooling section (6); 多个排料锥斗(9)设置在均匀进风装置(8)的下方;和A plurality of discharge cones (9) are arranged below the uniform air intake device (8); and 排料锥斗(9)的下方设有排料设备。A discharge device is provided below the discharge cone (9). 2.根据权利要求1所述的立式冷却机,其特征在于:在塔体内、热风出口(10)的前端设有辐射热回收器(F01);优选的是,辐射热回收器(F01)采用板翅型换热器或列管型换热器。2. The vertical cooling machine according to claim 1, characterized in that: in the tower body, the front end of the hot air outlet (10) is provided with a radiation heat recovery device (F01); preferably, the radiation heat recovery device (F01) A plate-fin heat exchanger or a tube-and-tube heat exchanger is used. 3.根据权利要求1或2所述的立式冷却机,其特征在于:排料设备为振动给料机(P)或板式给矿机(14);和/或3. The vertical cooler according to claim 1 or 2, characterized in that: the discharge device is a vibrating feeder (P) or a plate feeder (14); and/or 振动给料机(P)末端的下方设有冷烧结矿输送装置(11);优选的是,板式给矿机(14)的出料口下方设有排料溜槽或卸料斗(15),排料溜槽或卸料斗(15)的下方设有冷烧结矿输送装置(11)。A cold sinter conveying device (11) is provided below the end of the vibrating feeder (P); preferably, a discharge chute or a discharge hopper (15) is provided below the discharge port of the apron feeder (14). A cold sinter conveying device (11) is provided below the material chute or the discharge hopper (15). 4.根据权利要求1-3中任一项所述的立式冷却机,其特征在于:排料锥斗(9)的末端设有插板阀(12);和/或4. The vertical cooler according to any one of claims 1-3, characterized in that: the end of the discharge cone (9) is provided with a slide valve (12); and/or 冷却段(6)的下部(优选沿着圆周方向)设有测温探头(13);优选的是,所述测温探头(13)为热电偶温度传感器。The lower part of the cooling section (6) (preferably along the circumferential direction) is provided with a temperature measuring probe (13); preferably, the temperature measuring probe (13) is a thermocouple temperature sensor. 5.根据权利要求1-4中任一项所述的立式冷却机,其特征在于:均匀进风装置(8)包括环形或“C”形的外环进风管(801)、多个风道支管(802)和内环进风道(803),其中:环形或“C”形的外环进风管(801)设置在塔壁(5)的外侧周围,内环进风道(803)设置在塔体底部,每一个风道支管(802)的一端连接外环进风管(801)和另一端连接内环进风道(803);优选的是,内环进风道(803)的侧壁或侧面为百叶窗结构。5. The vertical cooling machine according to any one of claims 1-4, characterized in that: the uniform air inlet device (8) includes an annular or "C" shaped outer ring air inlet pipe (801), a plurality of The air duct branch pipe (802) and the inner ring air inlet duct (803), wherein: the ring or "C" shaped outer ring air inlet pipe (801) is arranged around the outer side of the tower wall (5), and the inner ring air inlet duct ( 803) is arranged at the bottom of the tower body, and one end of each air duct branch pipe (802) is connected to the outer ring air inlet pipe (801) and the other end is connected to the inner ring air inlet duct (803); preferably, the inner ring air inlet duct ( 803) the side wall or side is a louver structure. 6.根据权利要求1-5中任一项所述的立式冷却机,其特征在于:伞状溜槽(2)的分开段(202)的分支的数量和相应的竖直溜槽(3)的数量均为3-12个,优选为4-10个,更优选为6-8个。6. The vertical cooling machine according to any one of claims 1-5, characterized in that the number of branches of the split section (202) of the umbrella chute (2) and the number of branches of the corresponding vertical chute (3) The quantity is 3-12, preferably 4-10, more preferably 6-8. 7.根据权利要求1-6中任一项所述的立式冷却机,其特征在于:多个排料锥斗(9)在均匀进风装置(8)下端呈现环形分布或沿着圆周方向均匀地分布;和/或7. The vertical cooling machine according to any one of claims 1-6, characterized in that: a plurality of discharge cones (9) are distributed in a ring at the lower end of the uniform air inlet device (8) or along the circumferential direction evenly distributed; and/or 排料锥斗(9)的个数为4-12个,优选为6-10个,6-8个;和/或The number of discharge cones (9) is 4-12, preferably 6-10, 6-8; and/or 均匀进风装置(8)中风道支管(802)的数量2-12个,优选3-10个,更优选4-8个,更优选6-8个。The number of air duct branch pipes (802) in the uniform air inlet device (8) is 2-12, preferably 3-10, more preferably 4-8, more preferably 6-8. 8.根据权利要求5所述的立式冷却机,其特征在于:内环进风道(803)的顶端为封口和下端为开口;和/或8. The vertical cooling machine according to claim 5, characterized in that: the top end of the inner ring air inlet duct (803) is sealed and the lower end is an opening; and/or 均匀进风装置(8)包括1或2个内环进风道(803);优选的是,当有2个内环进风道(803)时,它们彼此上、下设置。The uniform air inlet device (8) includes 1 or 2 inner ring air inlet channels (803); preferably, when there are 2 inner ring air inlet channels (803), they are arranged above and below each other. 9.根据权利要求1-8中任一项所述的立式冷却机,其特征在于:排料设备为双层振动给料机(P);双层振动给料机(P)包括机体支架(P01)、上层振动槽(P02)、下层振动槽(P03)、振动器(P04);上层振动槽(P02)和下层振动槽(P03)设置在机体支架(P01)上,上层振动槽(P02)位于下层振动槽(P03)的上方,上层振动槽(P02)和下层振动槽(P03)分别与振动器(P04)连接;优选的是,上层振动槽(P02)和/或下层振动槽(P03)上设有调节装置(P05),调节装置(P05)调节下层振动槽(P03)的底板倾角优选的是,振动器(P04)包括上层振动器(P0401)和下层振动器(P0402),上层振动器(P0401)与上层振动槽(P02)连接,下层振动器(P0402)与下层振动槽(P03)连接;优选的是,上层振动槽(P02)和下层振动槽(P03)通过弹簧设置在机体支架(P01)上。9. The vertical cooling machine according to any one of claims 1-8, characterized in that: the discharge device is a double-layer vibrating feeder (P); the double-layer vibrating feeder (P) includes a body support (P01), the upper vibration tank (P02), the lower vibration tank (P03), the vibrator (P04); the upper vibration tank (P02) and the lower vibration tank (P03) are set on the body support (P01), the upper vibration tank ( P02) is located above the lower vibration tank (P03), the upper vibration tank (P02) and the lower vibration tank (P03) are respectively connected to the vibrator (P04); preferably, the upper vibration tank (P02) and/or the lower vibration tank (P03) is provided with an adjustment device (P05), and the adjustment device (P05) adjusts the bottom plate inclination angle of the lower vibration tank (P03). Preferably, the vibrator (P04) includes an upper vibrator (P0401) and a lower vibrator (P0402) , the upper vibrator (P0401) is connected to the upper vibrating tank (P02), and the lower vibrator (P0402) is connected to the lower vibrating tank (P03); preferably, the upper vibrating tank (P02) and the lower vibrating tank (P03) are connected by a spring Set on the body bracket (P01). 10.根据权利要求1-9中任一项所述的立式冷却机,其特征在于:该立式冷却机还包括控制系统(K),控制系统(K)与均匀进风装置(8)、冷烧结矿输送装置(11)、插板阀(12)、测温探头(13)、排料设备连接,并控制均匀进风装置(8)、冷烧结矿输送装置(11)、插板阀(12)、测温探头(13)、排料设备的操作。10. The vertical cooling machine according to any one of claims 1-9, characterized in that: the vertical cooling machine also includes a control system (K), the control system (K) and the uniform air inlet device (8) , cold sinter conveying device (11), inserting plate valve (12), temperature measuring probe (13), discharge equipment connection, and control uniform air intake device (8), cold sintering conveying device (11), inserting plate Operation of valve (12), temperature measuring probe (13), and discharge equipment. 11.一种烧结矿冷却方法或使用权利要求1-10中任一项所述的立式冷却机冷却烧结矿的方法,该方法包括以下步骤:11. A sinter cooling method or a method for cooling sinter using the vertical cooler according to any one of claims 1-10, the method comprising the following steps: (1)烧结矿进入立式冷却机的旋转布料器(1)内,在重力的作用下自上而下连续流动,经由伞状溜槽(2)进入竖直溜槽(3),然后堆积在冷却机的塔体内;(1) The sintered ore enters the rotary distributor (1) of the vertical cooler, flows continuously from top to bottom under the action of gravity, enters the vertical chute (3) through the umbrella chute (2), and then accumulates in the cooling machine tower body; (2)立式冷却机的均匀进风装置(8)输送冷却气体(例如空气)通过内环进风道(803)进入塔体内,冷却气体自下而上穿过堆积在塔体内的烧结矿料层,并与烧结矿进行逆流热交换,热交换后冷却气体温度逐渐升高,经立式冷却机塔内烧结矿料面排出,形成高温热风,高温热风经热风通道(7)从热风出口(10)排出;优选的是,高温热风被输送到余热利用系统(例如余热发电系统)中;(2) The uniform air intake device (8) of the vertical cooler transports cooling gas (such as air) into the tower body through the inner ring air inlet channel (803), and the cooling gas passes through the sintered ore accumulated in the tower body from bottom to top After the heat exchange, the temperature of the cooling gas gradually increases, and is discharged through the sinter material surface in the vertical cooling tower to form high-temperature hot air, which passes through the hot air channel (7) and exits the hot air outlet (10) discharge; preferably, the high-temperature hot air is delivered to a waste heat utilization system (such as a waste heat power generation system); (3)堆积在冷却机的塔体内的烧结矿与自下而上的冷却气体进行逆流热交换而被冷却,进入到立式冷却机下部的排料锥斗(9)中,然后由振动给料机(P)排出或由板式给矿机(14)经过排料溜槽或卸料斗(15)排出到冷烧结矿输送装置(11)上;和(3) The sintered ore accumulated in the tower body of the cooling machine is cooled by countercurrent heat exchange with the cooling gas from bottom to top, and enters the discharge cone (9) at the lower part of the vertical cooling machine, and then is fed by vibration. Discharged from the feeder (P) or from the apron feeder (14) to the cold sinter conveyor (11) through the discharge chute or discharge hopper (15); and (4)辐射热回收器(F01)回收烧结矿的辐射热能产生高温水蒸气,水蒸气通过热回收管道(F02)进入余热发电系统中。(4) The radiant heat recovery device (F01) recovers the radiant heat energy of the sinter to generate high-temperature water vapor, and the water vapor enters the waste heat power generation system through the heat recovery pipe (F02). 12.根据权利要求11所述的方法,其中根据测温探头(13)所检测的温度,控制系统(K)控制均匀进风装置(8)、冷烧结矿输送装置(11)、插板阀(12)、测温探头(13)、排料设备的操作,优选的是,其中与每一个排料锥斗(9)相对应在其上方设置测温探头(13),根据每一个测温探头(13)所检测的温度,控制系统(K)控制相对应的排料设备的操作。12. The method according to claim 11, wherein according to the temperature detected by the temperature measuring probe (13), the control system (K) controls the uniform air intake device (8), the cold sinter conveying device (11), the gate valve (12), the temperature measuring probe (13), the operation of the discharge equipment, preferably, wherein corresponding to each discharge cone (9), the temperature measuring probe (13) is set above it, according to each temperature measuring The temperature detected by the probe (13), the control system (K) controls the operation of the corresponding discharge equipment.
CN201710367694.6A 2017-05-23 2017-05-23 Vertical sinter cooler with rotary distributor and sinter cooling method Active CN108955276B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710367694.6A CN108955276B (en) 2017-05-23 2017-05-23 Vertical sinter cooler with rotary distributor and sinter cooling method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710367694.6A CN108955276B (en) 2017-05-23 2017-05-23 Vertical sinter cooler with rotary distributor and sinter cooling method

Publications (2)

Publication Number Publication Date
CN108955276A true CN108955276A (en) 2018-12-07
CN108955276B CN108955276B (en) 2023-07-04

Family

ID=64462445

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710367694.6A Active CN108955276B (en) 2017-05-23 2017-05-23 Vertical sinter cooler with rotary distributor and sinter cooling method

Country Status (1)

Country Link
CN (1) CN108955276B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112240710A (en) * 2020-11-02 2021-01-19 胡锡文 Vertical flow annular cooler for cement clinker
CN112474292A (en) * 2020-11-27 2021-03-12 陕西龙门钢铁有限责任公司 Device for secondary screening of blast furnace return ores in steel plant
CN113175822A (en) * 2021-04-30 2021-07-27 胡锡文 Pneumatic grading rotary cooler for cement clinker
CN116136361A (en) * 2023-04-20 2023-05-19 泽州县金秋铸造有限责任公司 Lifting type vertical cooling kiln cooling mechanism

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2668582A1 (en) * 1990-10-24 1992-04-30 Westfalia Becorit Ind Tech DEVICE FOR COOLING EXHAUSTED ANODES OF AN ELECTROLYTIC FUSION BATH.
WO2001067017A1 (en) * 2000-03-09 2001-09-13 Nkk Corporation Device for charging material into sintering machine
JP2008232519A (en) * 2007-03-20 2008-10-02 Mitsubishi-Hitachi Metals Machinery Inc Sinter cooling device
JP2009235551A (en) * 2008-03-28 2009-10-15 Jfe Steel Corp Heating-drying hopper for blast furnace raw materials, and method for adjusting temperature thereof
CN103234359A (en) * 2013-04-15 2013-08-07 中信重工机械股份有限公司 Sintering furnace type cooling device
CN104451140A (en) * 2013-09-13 2015-03-25 中冶东方工程技术有限公司秦皇岛研究设计院 Vertical cooling kiln
CN105021049A (en) * 2015-07-27 2015-11-04 宝鸡市晋旺达机械设备有限公司 Vertical cooling tower and sintering waste heat comprehensive utilization system
CN105066718A (en) * 2015-08-20 2015-11-18 宝鸡市晋旺达机械设备有限公司 Comprehensive utilization system for sintering waste heat
CN105605930A (en) * 2016-03-15 2016-05-25 宝钢工程技术集团有限公司 Air supply device and method for vertical type cooling furnace of sintered ore
CN106091707A (en) * 2016-06-23 2016-11-09 北京中冶设备研究设计总院有限公司 A kind of sintering deposit vertical adverse current waste-heat recovery device and method
CN106123572A (en) * 2016-08-10 2016-11-16 江苏垦乐节能环保科技有限公司 Multi-pipe discharge device of sinter shaft kiln waste heat recovery system
CN205897874U (en) * 2016-01-28 2017-01-18 中冶长天国际工程有限责任公司 Sealed blast air cooling device of slot type liquid for sintering deposit
CN106382823A (en) * 2016-08-30 2017-02-08 中信重工机械股份有限公司 Coupling energy saving device for multiple products of sintering procedure

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2668582A1 (en) * 1990-10-24 1992-04-30 Westfalia Becorit Ind Tech DEVICE FOR COOLING EXHAUSTED ANODES OF AN ELECTROLYTIC FUSION BATH.
US5182869A (en) * 1990-10-24 1993-02-02 Westfalia Becorit Industrietechnik Gmbh Apparatus for cooling spent anodes of electrolytic melting baths
WO2001067017A1 (en) * 2000-03-09 2001-09-13 Nkk Corporation Device for charging material into sintering machine
JP2008232519A (en) * 2007-03-20 2008-10-02 Mitsubishi-Hitachi Metals Machinery Inc Sinter cooling device
JP2009235551A (en) * 2008-03-28 2009-10-15 Jfe Steel Corp Heating-drying hopper for blast furnace raw materials, and method for adjusting temperature thereof
CN103234359A (en) * 2013-04-15 2013-08-07 中信重工机械股份有限公司 Sintering furnace type cooling device
CN104451140A (en) * 2013-09-13 2015-03-25 中冶东方工程技术有限公司秦皇岛研究设计院 Vertical cooling kiln
CN105021049A (en) * 2015-07-27 2015-11-04 宝鸡市晋旺达机械设备有限公司 Vertical cooling tower and sintering waste heat comprehensive utilization system
CN105066718A (en) * 2015-08-20 2015-11-18 宝鸡市晋旺达机械设备有限公司 Comprehensive utilization system for sintering waste heat
CN205897874U (en) * 2016-01-28 2017-01-18 中冶长天国际工程有限责任公司 Sealed blast air cooling device of slot type liquid for sintering deposit
CN105605930A (en) * 2016-03-15 2016-05-25 宝钢工程技术集团有限公司 Air supply device and method for vertical type cooling furnace of sintered ore
CN106091707A (en) * 2016-06-23 2016-11-09 北京中冶设备研究设计总院有限公司 A kind of sintering deposit vertical adverse current waste-heat recovery device and method
CN106123572A (en) * 2016-08-10 2016-11-16 江苏垦乐节能环保科技有限公司 Multi-pipe discharge device of sinter shaft kiln waste heat recovery system
CN106382823A (en) * 2016-08-30 2017-02-08 中信重工机械股份有限公司 Coupling energy saving device for multiple products of sintering procedure

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
天津天丰钢铁股份有限公司, 一种用于烧结矿冷却及显热高效回收利用系统 *
孙东;单士英;李晓艳;: "石横特钢180m~2烧结机提高成矿率的实践", 河北冶金, no. 12 *
赵斌;张玉柱;苍大强;路晓雯;张尉然;: "立式烧结冷却机与余热发电工艺研发", 烧结球团, no. 06 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112240710A (en) * 2020-11-02 2021-01-19 胡锡文 Vertical flow annular cooler for cement clinker
CN112474292A (en) * 2020-11-27 2021-03-12 陕西龙门钢铁有限责任公司 Device for secondary screening of blast furnace return ores in steel plant
CN113175822A (en) * 2021-04-30 2021-07-27 胡锡文 Pneumatic grading rotary cooler for cement clinker
CN113175822B (en) * 2021-04-30 2023-10-20 胡锡文 Cement clinker pneumatic grading rotary cooling machine
CN116136361A (en) * 2023-04-20 2023-05-19 泽州县金秋铸造有限责任公司 Lifting type vertical cooling kiln cooling mechanism

Also Published As

Publication number Publication date
CN108955276B (en) 2023-07-04

Similar Documents

Publication Publication Date Title
CN104451140A (en) Vertical cooling kiln
CN108955276A (en) Vertical sinter cooler and sinter cooling means with revolving top
CN205156639U (en) Vertical cooling system of sintering deposit
CN106556258A (en) Sintering mine sensible heat retracting device and its using method
CN105021049A (en) Vertical cooling tower and sintering waste heat comprehensive utilization system
CN108267013B (en) A sinter cooling and waste heat utilization system and low oxygen full cycle cooling method
CN206959601U (en) A kind of sintering deposit cooling and afterheat utilizing system
CN108955275A (en) Vertical sinter cooler and sinter cooling means with chute feeder
CN201277574Y (en) Flue dust conveyer used for tertiary air exhaust-heat boiler
CN108267018A (en) A kind of flashboard unloading type vertical cooling machine and sinter cooling means
CN206593486U (en) A kind of plate belt feeder unloading type vertical cooling machine
CN104121786B (en) Waste heat recovery furnace
CN109163569A (en) A kind of vertical sinter cooler of lattice and sinter cooling means
CN108931140A (en) Tower sinter cooler and sinter cooling means with fixed distribution device
CN206959414U (en) A kind of double furnace chambers drying oven heat extraction air cooling device
CN207779150U (en) The vertical accurate air feed control system of cooling furnace
CN206593485U (en) A kind of vertical sinter cooler
CN208980642U (en) Dry quenching furnace with inclined prestoring airflow channel and annular prestoring chamber
CN207716881U (en) A kind of vertical sinter cooler of lattice
CN207247920U (en) Vertical sinter cooler with revolving top
CN203451587U (en) Vertical cooling kiln
CN103629940B (en) Cooling device for annular cooling machine and annular cooling machine
CN108267019B (en) A vertical sinter cooler and sinter cooling method
CN109654893A (en) A kind of vertical cooling furnace of sinter air-draft-type and sinter cooling means
CN206891200U (en) There is the vertical sinter cooler of material position adjusting means

Legal Events

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