CN208810266U - The crush-grind system of clinker - Google Patents

The crush-grind system of clinker Download PDF

Info

Publication number
CN208810266U
CN208810266U CN201821086145.8U CN201821086145U CN208810266U CN 208810266 U CN208810266 U CN 208810266U CN 201821086145 U CN201821086145 U CN 201821086145U CN 208810266 U CN208810266 U CN 208810266U
Authority
CN
China
Prior art keywords
crusher
broken
batcher
fine
clinker
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
CN201821086145.8U
Other languages
Chinese (zh)
Inventor
杨少燕
何荣权
高立强
孙明俊
李淑菲
梅志
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.)
China ENFI Engineering Corp
Original Assignee
China ENFI Engineering Corp
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 China ENFI Engineering Corp filed Critical China ENFI Engineering Corp
Priority to CN201821086145.8U priority Critical patent/CN208810266U/en
Application granted granted Critical
Publication of CN208810266U publication Critical patent/CN208810266U/en
Priority to PCT/CN2019/088537 priority patent/WO2020010934A1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

The utility model discloses a kind of crush-grind system of clinker, which includes: coarse crushing unit, and the coarse crushing unit includes the clinker storehouse being sequentially connected, the first batcher and coarse crushing crusher, and the clinker storehouse is equipped with diagrid;In unit fine crushing, in described unit fine crushing include broken surge bunker in being sequentially connected, the second batcher, in broken crusher, vibrating screen, storage silo, third batcher and fine crusher, the vibrating screen is arranged in the top of the storage silo, surge bunker and fine ore bin are limited in the storage silo, the surge bunker is connected with the outlet of the oversize of the vibrating screen, the fine ore bin is connected with the screening outlet of the vibrating screen, it is described in broken surge bunker and the coarse crushing crusher and it is described in broken crusher be connected;Ore grinding unit, the ore grinding unit include that the 4th batcher being sequentially connected, ball mill, pump pond, Pulp pump and cyclone, the 4th batcher are connected with the fine ore bin.

Description

The crush-grind system of clinker
Technical field
The utility model belongs to ore dressing field, specifically, the utility model relates to the crush-grind systems of clinker.
Background technique
Broken and ore grinding is indispensable important component in clinker ore-dressing technique, is to improve technique of preparing economy The precondition of index.
Currently, being Semi-Autogenous device and traditional conventional disintegrating device in the Zha Xuan factory more universal disintegrating device of application. According to the statistical data of domestic and international clinker ore dressing, standard Bond's ball milling work index of clinker is generally 19kWh/t~23kWh/t.
Semi-Autogenous device generally comprises rough storehouse, semi-autogenous mill, ball mill, hydrocyclone, Pulp pump, belt conveying Machine.Semi-autogenous Grinding Technology is at home and abroad widely used in Cu-S ore ore dressing.Using Semi-Autogenous device, process is shorter, takes up an area face Product is small, but needs to carry out comminution test early period, and power consumption, steel ball consumption and liner plate consumption are higher, and production is easier to fluctuate, 0.5-1 is up to up to the period up to standard is produced.
Traditional conventional disintegrating device generally comprises product storage bin, gyratory crusher, vibrating screen, fine ore bin, ball mill, water Power cyclone, Pulp pump, belt conveyor.Process is longer, and production link is more, and dust pollution is more also easy to produce in production process, and The installation area is big, and Yi Zeng great project expropriation of land range increases construction cost.
Therefore, the comminution technology of existing clinker is further improved.
Utility model content
The utility model is intended to solve at least some of the technical problems in related technologies.For this purpose, this reality It is to propose a kind of crush-grind system of clinker with a novel purpose.The low 2-3kWh/t of the more Semi-Autogenous device of system power consumption, It can be foreshortened within 3 months up to period up to standard is produced, accounting of the obtained minus mesh partial size in 9-9.5mm is not less than 80%, and normal Rule disintegrating device is compared, and the utility model configuration is compact, occupied area is less.
In the one aspect of the utility model, the utility model proposes a kind of crush-grind systems of clinker, practical according to this Novel embodiment, the system include:
Coarse crushing unit, the coarse crushing unit include the clinker storehouse being sequentially connected, the first batcher and coarse crushing crusher, described Clinker storehouse is equipped with diagrid;
In unit fine crushing, it is described in unit fine crushing include broken surge bunker in being sequentially connected, the second batcher, in it is broken broken Machine, vibrating screen, storage silo, third batcher and fine crusher, the vibrating screen is arranged in the top of the storage silo, described Surge bunker and fine ore bin are limited in storage silo, the surge bunker is connected with the outlet of the oversize of the vibrating screen, the fine ore Storehouse is connected with the screening outlet of the vibrating screen, it is described in broken surge bunker and the coarse crushing crusher and it is described in broken crusher It is connected;
Ore grinding unit, the ore grinding unit include the 4th batcher being sequentially connected, ball mill, pump pond, Pulp pump and rotation Device is flowed, the 4th batcher is connected with the fine ore bin.
According to the crush-grind system of the clinker of the utility model embodiment, under the action of diagrid, may make broken into coarse crushing The clinker of broken machine is in reasonable particle size range;By the way that vibrating screen to be arranged in the top of storage silo, the minus mesh of vibrating screen is straight It taps into fine ore bin, oversize is directly entered surge bunker, thus can save screening workshop and 2 strip-type conveyers;Coarse crushing clinker Through further in it is broken and fine crushing after, can be obtained particle size range within the scope of 9-9.5mm accounting not less than 80% minus mesh, through into The overflow that partial size is not less than 65% less than 0.074mm accounting can be obtained after one step ore grinding;The more Semi-Autogenous device of whole system power consumption The consumption of low 2-3kWh/t, steel ball and liner plate is relatively low, and few using the test work load that this system need to carry out, up to production week up to standard Phase can foreshorten within 3 months, while operation is more stable, realizes the energy-efficient of system;Whole system can substantially reduce Occupied area and intermediate products are had bad luck, and the investment of building and ventilating and purifying air system is reduced, and produce more compact.
In addition, can also have following additional technology according to the crush-grind system of the clinker of the utility model above-described embodiment Feature:
Optional, the crush-grind system of above-mentioned clinker further comprises: the first belt conveyor, first belt conveyor Respectively with the coarse crushing crusher and it is described in broken surge bunker be connected, and first belt conveyor be equipped with weighing belt. Thus, it can be achieved that sending into the coarse crushing clinker in coarse crushing crusher to broken surge bunker.
Optional, the crush-grind system of above-mentioned clinker further comprises: the second belt conveyor, second belt conveyor Respectively with it is described in broken crusher, the fine crusher and the vibrating screen be connected.Thus, it can be achieved that by middle crushed slag and carefully Crushed slag is sent to vibrating screen.
Optional, the crush-grind system of above-mentioned clinker further comprises: third belt conveyor, the third belt conveyor It is connected respectively with the 4th batcher and the ball mill, and the third belt conveyor is equipped with weighing belt.As a result, It can be achieved through the 4th batcher to send minus mesh to ball mill.
Optional, the position of broken surge bunker and second belt are defeated in described on first belt conveyor The position on machine close to the vibrating screen is sent to be equipped with iron remover.This prevents crushers to cross iron.
Optional, first batcher is heavy-duty plate feeder, and the coarse crushing crusher is jaw crusher.By This, is conducive to the charge efficiency and coarse crushing effect that improve clinker.
It is optional, it is described in broken crusher be standard cone crusher, the fine crusher is short head cone crusher. Be conducive to effect broken and fine crushing in improving as a result,.
The additional aspect and advantage of the utility model will be set forth in part in the description, partially will be from following description In become obvious, or recognized by the practice of the utility model.
Detailed description of the invention
The above-mentioned and/or additional aspect and advantage of the utility model from the description of the embodiment in conjunction with the following figures will Become obvious and be readily appreciated that, in which:
Fig. 1 is the crush-grind system structural schematic diagram according to the clinker of the utility model one embodiment;
Fig. 2 is the crush-grind system structural schematic diagram according to the clinker of the utility model further embodiment;
Fig. 3 is the crush-grind system structural schematic diagram according to the clinker of the utility model another embodiment;
Fig. 4 is the crush-grind system structural schematic diagram according to the clinker of the utility model another embodiment;
Fig. 5 is the crush-grind system structural schematic diagram according to the clinker of the utility model another embodiment;
Fig. 6 is the comminution method stream for implementing clinker according to the crush-grind system using clinker of the utility model one embodiment Journey schematic diagram.
Specific embodiment
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by ginseng The embodiment for examining attached drawing description is exemplary, it is intended to for explaining the utility model, and should not be understood as to the utility model Limitation.
In the description of the present invention, it should be understood that term " center ", " longitudinal direction ", " transverse direction ", " length ", " width Degree ", " thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside", The orientation or positional relationship of the instructions such as " clockwise ", " counterclockwise ", " axial direction ", " radial direction ", " circumferential direction " is based on the figure Orientation or positional relationship is merely for convenience of describing the present invention and simplifying the description, rather than the dress of indication or suggestion meaning It sets or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as to the utility model Limitation.
In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or Implicitly include at least one this feature.The meaning of " plurality " is at least two, such as two in the description of the present invention, It is a, three etc., unless otherwise specifically defined.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " Gu It is fixed " etc. terms shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral;It can be Mechanical connection, is also possible to be electrically connected;It can be directly connected, two can also be can be indirectly connected through an intermediary The interaction relationship of connection or two elements inside element, unless otherwise restricted clearly.For the common skill of this field For art personnel, the concrete meaning of above-mentioned term in the present invention can be understood as the case may be.
In the present invention unless specifically defined or limited otherwise, fisrt feature is in the second feature " on " or " down " It can be that the first and second features directly contact or the first and second features are by intermediary mediate contact.Moreover, first is special Sign can be fisrt feature above the second feature " above ", " above " and " above " and be directly above or diagonally above the second feature, or only Indicate that first feature horizontal height is higher than second feature.Fisrt feature under the second feature " below ", " below " and " below " can be with It is that fisrt feature is directly under or diagonally below the second feature, or is merely representative of first feature horizontal height less than second feature.
In the one aspect of the utility model, the utility model proposes a kind of crush-grind systems of clinker, practical according to this Novel embodiment, with reference to Fig. 1, the system include: coarse crushing unit 100, in unit 200 and ore grinding unit 300 fine crushing.
Embodiment according to the present utility model, coarse crushing unit 100 include the clinker storehouse 110 being sequentially connected, the first batcher 120 and coarse crushing crusher 130, clinker storehouse 110 is equipped with diagrid 11, and is suitable for filtering out grain by the screening of diagrid in clinker storehouse The satisfactory clinker of diameter, then send to coarse crushing crusher through the first batcher and is crushed, to obtain coarse crushing clinker.Specifically , coarse crushing unit may be provided at slag and be crushed place boundary, so that broken clinker can transport clinker storehouse to frontloader;First gives Material machine is arranged in the bottom in clinker storehouse, and the first batcher can be heavy-duty plate feeder, and heavy-duty plate feeder is that one kind can The material of different grain size, different bulk density is conveyed to the conveying equipment of various material receiving devices, the machine be mainly used for from storage bin to Crusher, conveyer or other machinery be continuous and even feeding, it can also be used to and short distance conveys lumpiness and the biggish material of density, It is widely used in the industries such as mine, metallurgy, building materials, chemical industry, coal;Coarse crushing crusher can be jaw crusher, jaw crushing Machine structure is simple, and manufacture is easy, reliable operation.
One embodiment according to the present utility model, it is broken with jaw depending on the partial size of clinker is according to selected coarse crushing crusher For broken machine, jaw crusher divides according to feed inlet width size can be divided into three kinds of large, medium and small type, and feed inlet width is greater than 600mm is large machines, and feed inlet width is medium-sized machine in 300-600mm, and it is small-sized that feed inlet width, which is less than 300mm, Machine.When selecting medium-sized jaw crusher of the feed inlet width in 300-600mm, the partial size of the clinker filtered out through diagrid is just 600mm cannot be greater than.
The partial size of further embodiment according to the present utility model, the coarse crushing clinker after jaw crusher coarse crushing is not more than 160mm.This is determined by the gape size of jaw crusher.It is advantageously implemented as a result, broken in subsequent, saves the energy of system Consumption.
Embodiment according to the present utility model, in unit 200 fine crushing include broken surge bunker 210, second in being sequentially connected Batcher 220, in broken crusher 230, vibrating screen 240, storage silo 250, third batcher 260 and fine crusher 270, vibration The tops that sieve 240 is arranged in storage silo 250, limit surge bunker 251 and fine ore bin 252 in storage silo 250, surge bunker 251 with Vibrating screen 240 oversize outlet 241 be connected, fine ore bin 252 is connected with the screening outlet 242 of vibrating screen 240, in broken buffering Storehouse 210 and coarse crushing crusher 130 and in broken crusher 230 be connected, and be suitable for the coarse crushing clinker by in broken surge bunker through second Batcher send into broken crusher to be crushed, and to obtain middle crushed slag, middle crushed slag obtains partial size after vibrating screen sieves The minus mesh and the undesirable oversize of partial size, minus mesh for meeting subsequent ore grinding requirement send the fine ore into storage silo to store in a warehouse Deposit, oversize drop down onto surge bunker through third batcher send to fine crusher carry out it is fine crushing.Specifically, during the second batcher is located at The bottom of broken surge bunker, the second batcher can be belt feeder, and belt feeder has conveying capacity strong, conveying distance Far, the characteristics of structure is simply easy to maintain, can easily carry out Programmed control and automatic operation;In broken crusher can be Standard cone crusher, standard cone crusher reduction ratio is big, high-efficient, low energy consumption, and product granularity is uniform;Vibrating screen can be Mono-layer banana type vibrating screen passes through the exciting force for adjusting the upper and lower rotation weight of vibrating screen, thus it is possible to vary amplitude, and on adjusting, The space phase angle of lower heavy punch then can change the curve shape of compass screen surface motion profile and change the movement rail of material on compass screen surface Mark eliminates screening workshop and 2 bands to may make that oversize directly drops down onto surge bunker and minus mesh directly drops down onto fine ore bin Formula conveyer not only reduces investment but also can simplify production management;Surge bunker and fine ore bin can be two parts of storage silo, Can be the mutually independent component arranged in parallel of two sheets, fine ore bin can be circular flat bottom ore storage bin, can be used for adjusting muck with What is produced between ore grinding is unbalanced, so that subsequent ore grinding unit realizes steady production;Third batcher can be vibration Batcher, thus can in surge bunker material uniformly, be continuously given to fine crusher;Fine crusher broken crusher in Placed side by side, fine crusher can be short head cone crusher, with reduction ratio is big, high-efficient, treating capacity is high, operating cost It is low, easy to adjust, using it is economical the features such as.In space layout, in unit fine crushing be total to workshop against fine ore bin and arrange, and in it is broken Surge bunker be located at workshop it is secondary across.
One embodiment according to the present utility model, with reference to Fig. 2, in broken surge bunker 210 and coarse crushing crusher 130 pass through the One belt conveyor 280 is connected, and weighing belt 21 is equipped on the first belt conveyor 280.It thus can will be in coarse crushing crusher Coarse crushing clinker supply into broken surge bunker, while can be recorded by weighing belt carry out in processing fine crushing coarse crushing clinker amount, Realize the control to production.
Further embodiment according to the present utility model, with reference to Fig. 3, in broken crusher 230, fine crusher 270 pass through Second belt conveyor 290 is connected with vibrating screen 240.Middle crushed slag and clinker fine crushing can be passed through the second belt conveying as a result, Machine send to vibrating screen and is sieved, and further realizes and makes full use of to hall space position.One according to the present utility model Specific embodiment, the second belt conveyor may include 3 strip-type conveyers, and 3 strip-type conveyers cooperate, jointly broken by Clinker and clinker fine crushing are sent to vibrating screen.
Another embodiment according to the present utility model, with reference to Fig. 5, on the first belt conveyor 280 close in broken buffering Position on the position in storehouse 210 and the second belt conveyor 290 close to vibrating screen 240 is equipped with iron remover 22, and is suitable for the Carried out when one belt conveyor send coarse crushing clinker to the broken surge bunker into once except iron is handled and the second belt conveyor will in Crushed slag and/or clinker fine crushing carry out secondary except iron is handled when sending to vibrating screen.This prevents crushers to cross iron.
Another embodiment according to the present utility model, the partial size of minus mesh are that 9-9.5mm accounting is not less than 80%.By This, is conducive to the efficiency for improving subsequent grinding process.
Embodiment according to the present utility model, ore grinding unit 300 include the 4th batcher 310, the ball mill being sequentially connected 320, pond 330, Pulp pump 340 and cyclone 350, the 4th batcher 310 are pumped to be connected with fine ore bin 252, and is suitable for passing through the 4th Minus mesh is supplied into ball mill and carries out wet ground by batcher, and to obtain wet-milling ore pulp, wet-milling ore pulp is stored in pump pond, Cyclone is pumped to through slurry and carries out separating treatment, and to obtain overflow and sand setting, resulting sand setting is back to ball mill, gained Overflow send to subsequent floatation process.Specifically, the 4th batcher is located at fine ore bin bottom, the 4th batcher can be given for disk Material machine, disk feeder structure is simple, it is reliable for operation, adjust easy for installation and light-weight, small in size, reliable operation, service life Long, maintenance is conveniently.
One embodiment according to the present utility model, with reference to Fig. 4, the 4th batcher 310 and ball mill 320 pass through third band Formula conveyer 360 is connected, and third belt conveyor 360 is equipped with weighing belt 21, and being suitable for will by third belt conveyor Minus mesh from the 4th batcher, which is supplied into ball mill, carries out wet ground, and passes through the belt on third belt conveyor The amount of recordable lower minus mesh of the supply into grinding process of scale, to be conducive to control entire grinding process.
Further embodiment according to the present utility model, accounting of the partial size less than 0.074mm is not less than in eddy flow ore pulp 65%.Be conducive to improve the flotation efficiency of subsequent floatation process as a result,.
According to the crush-grind system of the clinker of the utility model embodiment, under the action of diagrid, may make broken into coarse crushing The clinker of broken machine is in reasonable particle size range;By the way that vibrating screen to be arranged in the top of storage silo, the minus mesh of vibrating screen is straight It taps into fine ore bin, oversize is directly entered surge bunker, thus can save screening workshop and 2 strip-type conveyers;Coarse crushing clinker Through further in it is broken and fine crushing after, can be obtained particle size range within the scope of 9-9.5mm accounting not less than 80% minus mesh, through into The overflow that partial size is not less than 65% less than 0.074mm accounting can be obtained after one step ore grinding;The more Semi-Autogenous device of whole system power consumption The consumption of low 2-3kWh/t, steel ball and liner plate is relatively low, and few using the test work load that this system need to carry out, up to production week up to standard Phase can foreshorten within 3 months, while operation is more stable, realizes the energy-efficient of system;Whole system can substantially reduce Occupied area and intermediate products are had bad luck, and the investment of building and ventilating and purifying air system is reduced, and produce more compact.
In order to facilitate understanding, the comminution method for implementing clinker to the crush-grind system using above-mentioned clinker below is retouched in detail It states, with reference to Fig. 6, this method comprises:
S100: the clinker in clinker storehouse is supplied by the first batcher to coarse crushing crusher and carries out coarse crushing
In the step, by the screening of diagrid in clinker storehouse, the satisfactory clinker of partial size is filtered out, is then given through first Material machine send to coarse crushing crusher and is crushed, to obtain coarse crushing clinker.
One embodiment according to the present utility model, it is broken with jaw depending on the partial size of clinker is according to selected coarse crushing crusher For broken machine, jaw crusher divides according to feed inlet width size can be divided into three kinds of large, medium and small type, and feed inlet width is greater than 600mm is large machines, and feed inlet width is medium-sized machine in 300-600mm, and it is small-sized that feed inlet width, which is less than 300mm, Machine.When selecting medium-sized jaw crusher of the feed inlet width in 300-600mm, the partial size of the clinker filtered out through diagrid is just 600mm cannot be greater than.
The partial size of further embodiment according to the present utility model, the coarse crushing clinker after jaw crusher coarse crushing is not more than 160mm.This is determined by the gape size of jaw crusher, is advantageously implemented as a result, broken in subsequent, saves the energy of system Consumption.
S200: by coarse crushing clinker through the second batcher supply into broken crusher carry out in it is broken, middle crushed slag is again through vibrating Sieve screening, oversize through third batcher supply to fine crusher carry out it is fine crushing, minus mesh is stored in fine ore bin
In the step, the coarse crushing clinker by in broken surge bunker send into broken crusher to be crushed through the second batcher, To obtain middle crushed slag, middle crushed slag obtains minus mesh and grain that partial size meets subsequent ore grinding requirement after vibrating screen sieves The undesirable oversize of diameter, minus mesh send the fine ore bin into storage silo to store, oversize drop down onto surge bunker through third to Material machine send fine crushing to fine crusher progress.
One embodiment according to the present utility model, the partial size of minus mesh are that 9-9.5mm accounting is not less than 80%.As a result, Be conducive to improve the efficiency of subsequent grinding process.
One embodiment according to the present utility model, middle crushed slag and clinker fine crushing are delivered to through the second belt conveyor Vibrating screen carries out screening process.As a result, can by middle crushed slag and clinker fine crushing by the second belt conveyor send to vibrating screen into Row screening, further realizes and makes full use of to hall space position.
S300: the minus mesh in fine ore bin is supplied through the 4th batcher to ball mill and carries out wet ground, wet-milling ore pulp It supplies through Pulp pump to cyclone and carries out separating treatment
In the step, minus mesh is supplied into ball mill by the 4th batcher and carries out wet ground, it is wet to obtain Ore grinding slurry, it is spare that wet-milling ore pulp is stored in pump pond, is pumped to cyclone through slurry and carries out separating treatment, to obtain overflow and heavy Sand, resulting sand setting are back to ball mill, and resulting overflow is sent to subsequent floatation process.
One embodiment according to the present utility model, accounting of the partial size less than 0.074mm is not less than 65% in overflow.By This, is conducive to the flotation efficiency for improving subsequent floatation process.
The comminution method for implementing clinker according to the crush-grind system using clinker of the utility model embodiment, in the work of diagrid Under, it may make the clinker into coarse crushing crusher in reasonable particle size range;By the way that vibrating screen is arranged in storage silo Top, the minus mesh of vibrating screen are directly entered fine ore bin, and oversize is directly entered surge bunker, thus can save screening workshop and 2 Strip-type conveyer;After coarse crushing clinker is broken and fine crushing in further, particle size range can be obtained, and accounting is not within the scope of 9-9.5mm The overflow that partial size is not less than 65% less than 0.074mm accounting can be obtained in minus mesh less than 80% after further ore grinding;Entirely The low 2-3kWh/t of the more Semi-Autogenous device of system power consumption, the consumption of steel ball and liner plate is relatively low, and the examination that need to be carried out using this system It is few to test workload, can be foreshortened within 3 months up to the period up to standard is produced, while operation is more stable, realizes the efficient section of system Energy;Whole system can substantially reduce having bad luck for occupied area and intermediate products, reduce the throwing of building and ventilating and purifying air system Money produces more compact.
It should be noted that feature and advantage described in the above-mentioned crush-grind system for clinker are equally applicable to the clinker Comminution method, details are not described herein again.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example Point is contained at least one embodiment or example of the utility model.In the present specification, to the schematic table of above-mentioned term It states and is necessarily directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be with It can be combined in any suitable manner in any one or more of the embodiments or examples.In addition, without conflicting with each other, this field Technical staff can by the feature of different embodiments or examples described in this specification and different embodiments or examples into Row combination and combination.
Although the embodiments of the present invention have been shown and described above, it is to be understood that above-described embodiment is Illustratively, it should not be understood as limiting the present invention, those skilled in the art are in the scope of the utility model Inside it can make changes, modifications, alterations, and variations to the above described embodiments.

Claims (7)

1. a kind of crush-grind system of clinker characterized by comprising
Coarse crushing unit, the coarse crushing unit include the clinker storehouse being sequentially connected, the first batcher and coarse crushing crusher, the clinker Storehouse is equipped with diagrid;
In unit fine crushing, it is described in unit fine crushing include broken surge bunker in being sequentially connected, the second batcher, in broken crusher, Vibrating screen, storage silo, third batcher and fine crusher, the vibrating screen is arranged in the top of the storage silo, described to deposit Surge bunker and fine ore bin are limited in warehouse, the surge bunker is connected with the outlet of the oversize of the vibrating screen, the fine ore bin Be connected with the screening outlet of the vibrating screen, it is described in broken surge bunker and the coarse crushing crusher and it is described in broken crusher phase Even;
Ore grinding unit, the ore grinding unit include the 4th batcher being sequentially connected, ball mill, pump pond, Pulp pump and cyclone, 4th batcher is connected with the fine ore bin.
2. system according to claim 1, which is characterized in that further comprise:
First belt conveyor, first belt conveyor respectively with the coarse crushing crusher and it is described in broken surge bunker phase Even, and first belt conveyor is equipped with weighing belt.
3. system according to claim 1 or 2, which is characterized in that further comprise:
Second belt conveyor, second belt conveyor respectively with it is described in broken crusher, the fine crusher and institute Vibrating screen is stated to be connected.
4. system according to claim 1, which is characterized in that further comprise:
Third belt conveyor, the third belt conveyor are connected with the 4th batcher and the ball mill respectively, and And the third belt conveyor is equipped with weighing belt.
5. system according to claim 3, which is characterized in that broken slow in described on first belt conveyor It rushes the position on the position and second belt conveyor in storehouse close to the vibrating screen and is equipped with iron remover.
6. system according to claim 1, which is characterized in that first batcher is heavy-duty plate feeder, described Coarse crushing crusher is jaw crusher.
7. system according to claim 1, which is characterized in that broken crusher is standard cone crusher in described, described Fine crusher is short head cone crusher.
CN201821086145.8U 2018-07-10 2018-07-10 The crush-grind system of clinker Active CN208810266U (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201821086145.8U CN208810266U (en) 2018-07-10 2018-07-10 The crush-grind system of clinker
PCT/CN2019/088537 WO2020010934A1 (en) 2018-07-10 2019-05-27 Grinding system and method for slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821086145.8U CN208810266U (en) 2018-07-10 2018-07-10 The crush-grind system of clinker

Publications (1)

Publication Number Publication Date
CN208810266U true CN208810266U (en) 2019-05-03

Family

ID=66270692

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821086145.8U Active CN208810266U (en) 2018-07-10 2018-07-10 The crush-grind system of clinker

Country Status (1)

Country Link
CN (1) CN208810266U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108745593A (en) * 2018-07-10 2018-11-06 中国恩菲工程技术有限公司 The crush-grind system and method for clinker
WO2020010934A1 (en) * 2018-07-10 2020-01-16 中国恩菲工程技术有限公司 Grinding system and method for slag

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108745593A (en) * 2018-07-10 2018-11-06 中国恩菲工程技术有限公司 The crush-grind system and method for clinker
WO2020010934A1 (en) * 2018-07-10 2020-01-16 中国恩菲工程技术有限公司 Grinding system and method for slag

Similar Documents

Publication Publication Date Title
CN108745593A (en) The crush-grind system and method for clinker
CN202438372U (en) Quartz smashing graded production line
CN102950055B (en) Calcium carbonate slurry wet grinding manufacture method
US9839915B2 (en) Impact grinding plant for the communition of ore
CN208810266U (en) The crush-grind system of clinker
CN101862699A (en) Semi-finished pre-grinding vertical-milling and ball-milling combined grinding device
CN109046719A (en) Crush-grind system and method
CN102059172A (en) Ore milling method for vanadium-titanium magnetite ore
Jankovic Developments in iron ore comminution and classification technologies
CN107661814B (en) Screening-magnetic separation-ore grinding-magnetic separation flow equipment arrangement system
US4109871A (en) Method and apparatus for processing abrasive material
CN111921697A (en) Method and equipment for complex copper-lead-zinc sulphide ore crushing and grinding process
CN111822129A (en) Iron ore dry grinding and dressing device and process
CN213050984U (en) Crushing and grinding process technological equipment
CN212468837U (en) Combined type discharging hopper for gravel aggregate
CN212820408U (en) Vertical mill grinding system for grinding weak-magnetic refractory iron ore
CN101161349B (en) Ore-sorting system and technique for iron ore powder
CN100361749C (en) Crushing method and apparatus
CN106238188B (en) Respective grinding process at times
CN101972684A (en) Prescreening mechanism of single-section hammer type screening crusher
CN208944319U (en) Crush-grind system
CN202909806U (en) Wet grinding equipment for calcium carbonate slurry
CN103157543A (en) Alumina crust block crushing process and production line thereof
CN210159764U (en) Coarse grain wet type pre-magnetic separation and closed circuit ore grinding grading system in HPGR flow
CN210411073U (en) High-efficient ore crushing system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant