CN204933628U - A kind of ore reduction screening blending system - Google Patents
A kind of ore reduction screening blending system Download PDFInfo
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- CN204933628U CN204933628U CN201520313364.5U CN201520313364U CN204933628U CN 204933628 U CN204933628 U CN 204933628U CN 201520313364 U CN201520313364 U CN 201520313364U CN 204933628 U CN204933628 U CN 204933628U
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- 238000012216 screening Methods 0.000 title claims abstract description 77
- 238000002156 mixing Methods 0.000 title claims abstract description 56
- 238000003860 storage Methods 0.000 claims abstract description 75
- 238000007873 sieving Methods 0.000 claims abstract description 19
- 238000000227 grinding Methods 0.000 claims abstract description 16
- 239000000428 dust Substances 0.000 claims description 41
- 238000007689 inspection Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 5
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 15
- 229910052500 inorganic mineral Inorganic materials 0.000 description 14
- 239000000463 material Substances 0.000 description 14
- 239000011707 mineral Substances 0.000 description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 13
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 229910052742 iron Inorganic materials 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 238000005065 mining Methods 0.000 description 5
- 238000009826 distribution Methods 0.000 description 4
- 238000013467 fragmentation Methods 0.000 description 4
- 238000006062 fragmentation reaction Methods 0.000 description 4
- 230000008450 motivation Effects 0.000 description 4
- 229910052681 coesite Inorganic materials 0.000 description 3
- 229910052906 cristobalite Inorganic materials 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000005453 pelletization Methods 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 235000012239 silicon dioxide Nutrition 0.000 description 3
- 229910052682 stishovite Inorganic materials 0.000 description 3
- 229910052905 tridymite Inorganic materials 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000010410 dusting Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241000282376 Panthera tigris Species 0.000 description 1
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000002457 bidirectional effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
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- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
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Abstract
The utility model relates to a kind of ore reduction screening blending system, comprises crushing system, screening system and blending system; Wherein, blending system comprises fine ore mixing ore storage bin, the heap storage of lump ore ore deposit and entrucking ore storage bin, and entrucking ore storage bin and fine ore are mixed ore storage bin and be connected by belt feeder.Crushing system comprises raw ore storage warehouse, coarse crushing device, middle grinding and sieving device, ore is transported to coarse crushing device by belt feeder by raw ore storage warehouse, ore is sieve screening system in small, broken bits in being transported to by belt feeder after coarse crushing device, is transported to fine ore respectively mixes ore storage bin and the heap storage of lump ore ore deposit during ore passes through after sieve screening system in small, broken bits by belt feeder; Screening system mixes ore storage bin with fine ore respectively by belt feeder and the heap storage of lump ore ore deposit is connected.Compared with prior art, ore reduction that the utility model provides screening blending system have safeguard simple, maintenance is convenient, production operation is easy, the effect that daily operation cost is low.
Description
Technical field
The utility model relates to ore sizing technical field, especially relates to a kind of ore reduction screening blending system.
Background technology
Although Mineral Resources in China total amount is enriched, of a great variety, belong to third place in the world mining powers, occupancy volume per person is only world occupancy volume per person's 58%, is in the 53rd.Along with China's sustain economic, develop rapidly, process of industrialization is accelerated, and to the absolute magnitude of mineral resources demand in continuous increase, the imbalance between supply and demand of mineral resources manifested in recent years.China's economic in decades from now on, period that social development is the fastest to mineral resources demand growth, estimate that Mineral Resources in China demand will peak in mid-term in this century, have some important mineral products will sink into critical shortage situation.In the past in 10 years, output and the consumption of Chinese mineral products all maintain positive growth, and pig iron consumption figure increases by 8.1% every year, and steel consumption figure increases by 9% every year, and aluminium consumption figure increases by 11.6% every year.China establishes mineral trade relation with more than 100 countries, and mineral products import increases by 11.7% every year, within 2002, reaches 58,700,000,000 dollars.The first half of the year in 2003, Chinese imported Fe ore increases by 45% on year-on-year basis, and import copper increases by 40% on year-on-year basis, accounts for 20% of import market, world share, and the demand of China and supply directly affect Global Mining Industry and produce.The solid demand of China to mineral resources, has driven the development of World Mining Industry.Chinese Enterprises holds economic globalization opportunity simultaneously, implements global stratege o f resources, goes abroad, set up Strategic Mineral Resources deposit and security provisions system.What World Mining Industry was produced becomes increasingly prosperous, and adds the demand to mining equiment.
Ore, after being broken, often will utilize the working face of porous that mixtures different for granular size is carried out graded operation by its granular size, Here it is screening operation.
Screening operation can under wet condition (containing more moisture, add water on compass screen surface or submergence in the sink) carry out, this operation is called wet screening, and what adopt at present extensively is the dry type screening operation do not added water.
The task of screening: screening operation is widely used for ore dressing plant and screening factory, and the screen(ing) machine task of bearing in whole flow process is normal not identical, according to the difference of application purpose and use occasion, screening operation can be divided into several.Independent screening is called when sieving product and using as final products supply user.When screening is for being called preliminary screening when sorting the selected material providing size fractionated, as the sieve classification of material before gravity treatment and magnetic separation, when sieve with broken with the use of time be called auxiliary screening, if material qualified for granularity separates in advance by it before broken, cry prescreening, if for the granularity of controlled fragmentation product, cry check screening, meanwhile, can also play in advance and check screening effect by a screening operation simultaneously.Screening also can be used to remove the moisture in material or is separated ore pulp, as the dehydration of coal separation and washup product and heavymedia separation product removal medium etc.In some cases, the quality of screening product is different, and the effect of sorting valuable mineral is played in screening, and this screening claims to select screening.Fine sizing as many iron ore factories iron ore concentrate is regrinded in circulation at present just rises selects sieving actoion, improves the grade of iron ore concentrate with dusting cover.Along with the development of material sieving technology and screening plant, the purposes of screening is also expanding gradually.
But often existing defects in existing ore reduction screening blending system, the shortcomings such as such as screening efficiency is low, energy consumption is high, floor space is excessive.
In view of this, special proposition the utility model.
Utility model content
The purpose of this utility model is to provide a kind of a kind of ore reduction screening blending system that can overcome above-mentioned defect.
A kind of ore reduction screening blending system that the utility model provides, its specific implementation is as follows:
A kind of ore reduction screening blending system, comprises crushing system, screening system and blending system;
Wherein, described blending system comprises fine ore mixing ore storage bin, the heap storage of lump ore ore deposit and entrucking ore storage bin, and described entrucking ore storage bin and described fine ore are mixed ore storage bin and be connected by belt feeder.
Described crushing system comprises raw ore storage warehouse, coarse crushing device, middle grinding and sieving device, ore is transported to described coarse crushing device by described belt feeder by described raw ore storage warehouse, ore is sieve screening system in small, broken bits in being transported to by described belt feeder after coarse crushing device, is transported to described fine ore respectively mixes ore storage bin and described lump ore ore deposit heap storage during ore passes through after sieve screening system in small, broken bits by described belt feeder;
Described screening system mixes ore storage bin with described fine ore respectively by described belt feeder and described lump ore ore deposit heap storage is connected.
Preferably, entrucking ore storage bin has oscillating feeder.
Preferably, the described belt feeder be connected between described coarse crushing device with described middle grinding and sieving device is provided with magnetic ore deferrization device.
Preferably, described crushing system also comprises the bar screen before being arranged on described coarse crushing device, described ore is after described bar screen, ore on described bar screen sieve is transported to described coarse crushing device, and the ore under described bar screen sieve is transported to described middle grinding and sieving device by described belt feeder.
Preferably, front vibratory sieve in small, broken bits, intermediate crusher, fine crusher, surge bunker during described middle grinding and sieving device comprises, ore is by after front vibratory sieve in small, broken bits in described, ore in described on front Vibration Screen in small, broken bits is transported to described intermediate crusher and described fine crusher respectively by described belt feeder, in described under front Vibration Screen in small, broken bits, described intermediate crusher, described fine crusher be all connected with described surge bunker by described belt feeder, described surge bunker by described belt feeder be transported to described in front vibratory sieve in small, broken bits formed closed circuit;
Be connected with described lump ore ore deposit heap storage by described belt feeder in front Vibration Screen in small, broken bits in described; Also mix ore storage bin by described belt feeder and described fine ore under front Vibration Screen in small, broken bits in described to be connected.
Preferably, described coarse crushing device is jaw crusher.
Preferably, also truck scale is provided with at described entrucking ore storage bin entrance and the outlet of described fine ore mixing ore storage bin; Described belt feeder is provided with belt conveyer scale.
Preferably, also dust arrester is provided with in described crushing system and described screening system.
Preferably, described dust arrester is sack cleaner.
Preferably, in described crushing system, described screening system and described blending system, also automatic inspection device is provided with.
Compared with prior art, ore reduction that the utility model provides screening blending system have safeguard simple, maintenance is convenient, production operation is easy, the effect that daily operation cost is low.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model detailed description of the invention or technical scheme of the prior art, be briefly described to the accompanying drawing used required in detailed description of the invention or description of the prior art below, apparently, accompanying drawing in the following describes is embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
The structural representation of a kind of ore reduction screening blending system that Fig. 1 provides for the utility model embodiment;
The structural representation of entrucking ore storage bin in a kind of ore reduction screening blending system that Fig. 2 provides for the utility model embodiment.
Detailed description of the invention
Be clearly and completely described the technical solution of the utility model below in conjunction with accompanying drawing, obviously, described embodiment is the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
In description of the present utility model, it should be noted that, orientation or the position relationship of the instruction such as term " " center ", " on ", D score, "left", "right", " vertically ", " level ", " interior ", " outward " they be based on orientation shown in the drawings or position relationship; be only the utility model and simplified characterization for convenience of description; instead of instruction or imply the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore can not be interpreted as restriction of the present utility model.In addition, term " first ", " second ", " the 3rd " only for describing object, and can not be interpreted as instruction or hint relative importance.
In description of the present utility model, it should be noted that, unless otherwise clearly defined and limited, term " installation ", " being connected ", " connection " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or connect integratedly; Can be mechanical connection, also can be electrical connection; Can be directly be connected, also indirectly can be connected by intermediary, can be the connection of two element internals.For the ordinary skill in the art, concrete condition the concrete meaning of above-mentioned term in the utility model can be understood.
As shown in Figure 1, the utility model embodiment provides a kind of ore reduction to sieve blending system, comprises crushing system, screening system and blending system;
Wherein, described blending system comprises fine ore mixing ore storage bin 4, lump ore ore deposit heap storage 2 and entrucking ore storage bin 1, and described entrucking ore storage bin and described fine ore are mixed ore storage bin and be connected by belt feeder 3.
Described crushing system comprises raw ore storage warehouse 5, coarse crushing device 6, middle grinding and sieving device 7, ore is transported to described coarse crushing device by described belt feeder by described raw ore storage warehouse, ore is sieve screening system in small, broken bits in being transported to by described belt feeder after coarse crushing device, is transported to described fine ore respectively mixes ore storage bin and described lump ore ore deposit heap storage during ore passes through after sieve screening system in small, broken bits by described belt feeder;
Described screening system mixes ore storage bin with described fine ore respectively by described belt feeder and described lump ore ore deposit heap storage is connected.
Ore reduction that the utility model provides screening blending system have safeguard simple, maintenance is convenient, production operation is easy, the effect that daily operation cost is low.
Crushing system particularly in the utility model comprises coarse crushing device and middle grinding and sieving device, can farthest make the granular size of ore reach needed for production by coarse crushing, middle fragmentation, these three kinds of crumbling methods of fine crushing.
There is provided a kind of ore reduction to sieve blending system at the utility model preferred embodiment as shown in Figure 2, entrucking ore storage bin has oscillating feeder 12.
In the utility model, ore by being transported in entrucking ore storage bin by belt feeder from fine ore mixing ore storage bin, mine car entrucking can be given very easily by the oscillating feeder under entrucking ore storage bin, improve the automaticity of production, decrease artificial operation.With in the past by a dead lift or scraper on mine car, substantially increase production efficiency.
There is provided a kind of ore reduction to sieve blending system at the utility model preferred embodiment, the described belt feeder be connected between described coarse crushing device with described middle grinding and sieving device is provided with magnetic ore deferrization device.
By being arranged on assorted iron in the magnetic ore deferrization device removing tcrude ore on belt feeder in the utility model, assorted iron can be avoided the infringement of disintegrating machine, improve the service life of equipment.
A kind of ore reduction is provided to sieve blending system at the utility model preferred embodiment, described crushing system also comprises the bar screen before being arranged on described coarse crushing device, described ore is after described bar screen, ore on described bar screen sieve is transported to described coarse crushing device, and the ore under described bar screen sieve is transported to described middle grinding and sieving device by described belt feeder.
The utility model increases a bar screen before coarse crushing device, can be preliminary ore be sieved, described coarse crushing device is transported at the ore on described bar screen sieve, ore under described bar screen sieve is transported to described middle grinding and sieving device by described belt feeder, can process for the ore of variable grain size like this, improve the production efficiency of coarse crushing device and middle grinding and sieving device, also improve the production efficiency of overall ore reduction screening blending system.
A kind of ore reduction is provided to sieve blending system at the utility model preferred embodiment, front vibratory sieve in small, broken bits during described middle grinding and sieving device comprises, intermediate crusher, fine crusher, surge bunker, ore is by after front vibratory sieve in small, broken bits in described, ore in described on front Vibration Screen in small, broken bits is transported to described intermediate crusher and described fine crusher respectively by described belt feeder, in described under front Vibration Screen in small, broken bits, described intermediate crusher, described fine crusher is all connected with described surge bunker by described belt feeder, described surge bunker by described belt feeder be transported to described in front vibratory sieve in small, broken bits formed closed circuit,
Be connected with described lump ore ore deposit heap storage by described belt feeder in front Vibration Screen in small, broken bits in described; Also mix ore storage bin by described belt feeder and described fine ore under front Vibration Screen in small, broken bits in described to be connected.
In the utility model, breaker in small, broken bits front vibratory sieve in small, broken bits, intermediate crusher, fine crusher, surge bunker in comprising in described, and front vibratory sieve in small, broken bits, intermediate crusher, fine crusher, surge bunker define closed cycle in this, the ore that can ensure to be delivered to institute's ore deposit mixing ore storage bin and the heap storage of lump ore ore deposit like this meets granular size and requires, ensures to some extent the quality of product.
There is provided a kind of ore reduction to sieve blending system at the utility model preferred embodiment, described coarse crushing device is jaw crusher.
In the utility model, jaw crusher fragmentation work presses to fixed jaw periodically by moving jaw plate, crushed by the material be clipped between two jaws.According to the track of dynamic jaw movement, simple single toggle jaw crusher and complicated swing jaw crushing apparatus can be divided into.Jaw crusher is commonly called as " tiger mouth ", is one of time-honored disintegrating machine, is still the most effective equipment of broken hard material so far.
Certain coarse crushing device, except making jaw crusher, can also be gyratory crusher, kibbler roll, impact crusher, grater etc., therefore according to the difference of production technology and actual working environment, can select different coarse crushing devices.As long as so the device that can meet coarse crushing object all belongs within the scope that the utility model protects.
There is provided a kind of ore reduction to sieve blending system at the utility model preferred embodiment, be also provided with truck scale at described entrucking ore storage bin entrance and the outlet of described fine ore mixing ore storage bin; Described belt feeder is provided with belt conveyer scale.
The utility model is by installing truck scale 11 at raw ore storage warehouse entrance, and object carries out raw material metering by truck scale before tcrude ore enters system; For ease of grasping production capacity; Belt feeder installs belt conveyer scale, and object to weigh ore or fine ore at any time; The outlet of fine ore mixing ore storage bin arranges truck scale, and object before going out system, carries out finished product metering at ore or fine ore by truck scale, to understand the production efficiency of system.
There is provided a kind of ore reduction to sieve blending system at the utility model preferred embodiment, in described crushing system and described screening system, be also provided with dust arrester.
Ore produces a large amount of technique dust in fragmentation, screening and belt transport process.For iron ore, main harmful components that are broken, screening plant dust are free SiO2s, wherein coarse crushing device dust free SiO2 content is 11.48% ~ 41.28%, in breaker dust free SiO2 content in small, broken bits be 24.49% ~ 32.69%, screening system dust free SiO2 content is 33.05% ~ 40.22%.
Need take effective synthesis dust prevention measure to all kinds of airborne dust points in technical process, the equipping rules of dust arrester is as follows:
(1) to each product dirt pits, according to size and the concrete condition of sending dust, undertaken airtight by technology major.
(2), allow the condition of water content in technique under, hydraulic dust-removing nozzle is adopted to carry out maximum humidification to material.
(3) on the basis of airtight and hydraulic dust-removing, dust removal with machine system is set.
(4) for preventing reentrainment of dust, water flushing device can be set in system; Material humidification controls the most effective means that mineral process produces dust, at non-heating season joint, according to material properties and allow maximum water capacity, from by mineral resources head, each section of belt material feeding point established to hydraulic dust-removing nozzle depositing dust and added wet stock.
Arranging of dust removal with machine equipment can according to local climate feature, to ore processing, the dust removal with machine system of delivery technology process selects sack cleaner.The device less to dedusting air quantity, selects bag pulse dedusting unit; The device moderate to dedusting air quantity, selects gas tank type pulse bag dust collector; The device larger to dedusting air quantity, selects long bag low-pressure pulse bag filter.3 kinds of deduster purification efficiencies all reach 99.5%.
In the utility model embodiment, consider that qualified raw ore sand product does not need processing, directly can enter fine ore mixing ore storage bin, it is more reasonable that dust pelletizing system is set separately.
Fine ore mixing ore storage bin dust pelletizing system dedusting air quantity adds up to 16000m3/h, and pipe-line system resistance is about 1370Pa.The initial dust content 8g/Nm3 of gas.Select PPCS64-5 type gas tank type pulse bag dust collector 1, filter area 310m2, resistance 1700Pa, complete machine power 5.5kW, voltage 380V.
G4-73 № type 8C centrifugal fan joined by deduster, the air quantity 24560m3/h of blower fan, total head 3260Pa, revolution 1800r/min, right 45 °; Distribution motivation Y200L2-2 type, power 37kW, voltage 380V.Hydraulic dust-removing nozzle is established to add wet stock on groove top, ore deposit.At belt feeder material feeding point place, if hydraulic dust-removing floral tube adds wet stock.The dust that deduster is collected returns technique belt on the spot.
In an embodiment of the present utility model, raw ore storage warehouse, coarse crushing device are more close, close and establish 1 dust pelletizing system more reasonable.
Dedusting air quantity adds up to 31000m3/h, and pipe-line system resistance is about 1500Pa.The initial dust content 8g/Nm3 of gas.Select PPCS96-2x5 biserial gas tank type pulse bag dust collector 1, filter area 929m2, resistance 1700Pa, complete machine power 15kW, voltage 380V.
G4-73 № type 11D centrifugal fan joined by deduster, the air quantity 47427m3/h of blower fan, total head 3986Pa, revolution 1450r/min, right 45 °; Distribution motivation Y280M-4 type, power 90kW, voltage 380V.Establish hydraulic dust-removing nozzle to add wet stock on groove top, ore deposit, water consumption is 4.0t/h.
In raw ore storage warehouse, coarse crushing device place and lower belt material feeding place, if hydraulic dust-removing floral tube adds wet stock, water consumption is 3t/h × 3.
The dust that deduster is collected returns technique belt on the spot.
In the utility model embodiment, in breaker dedusting air quantity in small, broken bits add up to 103000m3/h, pipe-line system resistance is about 2000Pa.The initial dust content 8g/Nm3 of gas.Select the long bag pulsed jet cloth filter of LLP-2250 1, filter area 2250m2, resistance 1700Pa, reserved complete machine power 28kW, voltage 380V.
G4-73 № type 18D centrifugal fan joined by deduster, the air quantity 154160m3/h of blower fan, total head 4639Pa, revolution 960r/min, left 45 °; Distribution motivation Y4508-6 type, power 315kW, voltage 10000V.
In breaker material inlet in small, broken bits, middle dusting cover divide total belt feeder discharging point place, if hydraulic dust-removing floral tube adds wet stock, water consumption is 2t/h × 5.
Deduster platform lower is established between dedusting control device and air compressor machine.2, SA75A air compressor is established in air compressor machine.Air demand 14.5L/min/ platform.
The dust that deduster is collected returns technique belt through 2 D400 screw machines.
In the utility model embodiment, screening system dedusting air quantity adds up to 60000m3/h, and pipe-line system resistance is about 1800Pa.The initial dust content 8g/Nm3 of gas.Select the long bag pulsed jet cloth filter of LLP-1360 1, filter area 1360m2, resistance 1700Pa, reserved complete machine power 22kW, voltage 380V.
G4-73 № type 12D centrifugal fan joined by deduster, the air quantity 92500m3/h of blower fan, total head 4047Pa, revolution 1450r/min, left 45 °; Distribution motivation Y315M1-6 type, power 160kW, voltage 380V.
Sieve total belt feeder discharging point place, if hydraulic dust-removing floral tube adds wet stock, water consumption is 2t/h × 2.
The dust that deduster is collected returns technique belt through 2 D400 screw machines.
Less by ore deposit groove dedusting air quantity, establish deduster separately.Airborne dust point dedusting air quantity is 8000m3/h, and pipe-line system resistance is 1000Pa.The initial dust content 8g/Nm3 of gas.Select PPCS32-5 gas tank type pulse bag dust collector 1.The filter area 155m2 of deduster, working resistance 1450Pa, dust removal unit complete machine power 10kW, voltage 380V.Deduster deashing adopts timing controlled mode, and defeated ash adopts timing controlled mode.
Dust removal machine assembly 4-68 № 5A centrifugal blower air quantity 10197m3/h, total head 3187Pa, rotating speed 2900r/min, blower motor Y160M2-2 type, N=15kW, voltage 380V.
The dust that deduster is collected returns technique belt on the spot.
In an embodiment of the present utility model, described dust arrester is sack cleaner.
In an embodiment of the present utility model, in described crushing system, described screening system and described blending system, be also provided with automatic inspection device.
The utility model by automatic inspection device 13 can very convenient when system jam the very first time recognize equipment Problems existing, and can very fast equipment fault be overhauled, substantially increase production efficiency.
In an embodiment of the present utility model, screening system comprises by ore deposit groove 9 and screening machine 8, describedly to be connected by belt feeder with described screening machine 8 by ore deposit groove 9, described screening machine mixes ore storage bin by Bidirectional belt conveyor and fine ore, raw ore sand unloads ore storage bin 10 and is connected, namely the ore in sifted is transported to raw ore sand and unloads ore storage bin, and the ore under sifted is transported to fine ore mixing ore storage bin.
Last it is noted that above each embodiment is only in order to illustrate the technical solution of the utility model, be not intended to limit; Although be described in detail the utility model with reference to foregoing embodiments, those of ordinary skill in the art is to be understood that: it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein some or all of technical characteristic; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the scope of each embodiment technical scheme of the utility model.
Claims (10)
1. an ore reduction screening blending system, is characterized in that, comprise crushing system, screening system and blending system;
Wherein, described blending system comprises fine ore mixing ore storage bin, the heap storage of lump ore ore deposit and entrucking ore storage bin, and described entrucking ore storage bin and described fine ore are mixed ore storage bin and be connected by belt feeder;
Described crushing system comprises raw ore storage warehouse, coarse crushing device, middle grinding and sieving device, ore is transported to described coarse crushing device by described belt feeder by described raw ore storage warehouse, ore is sieve screening system in small, broken bits in being transported to by described belt feeder after coarse crushing device, is transported to described fine ore respectively mixes ore storage bin and described lump ore ore deposit heap storage during ore passes through after sieve screening system in small, broken bits by described belt feeder;
Described screening system mixes ore storage bin with described fine ore respectively by described belt feeder and described lump ore ore deposit heap storage is connected.
2. ore reduction screening blending system according to claim 1, it is characterized in that, entrucking ore storage bin has oscillating feeder.
3. ore reduction screening blending system according to claim 2, is characterized in that, the described belt feeder be connected between described coarse crushing device with described middle grinding and sieving device is provided with magnetic ore deferrization device.
4. ore reduction screening blending system according to claim 3, it is characterized in that, described crushing system also comprises the bar screen before being arranged on described coarse crushing device, described ore is after described bar screen, ore on described bar screen sieve is transported to described coarse crushing device, and the ore under described bar screen sieve is transported to described middle grinding and sieving device by described belt feeder.
5. ore reduction screening blending system according to claim 4, it is characterized in that, front vibratory sieve in small, broken bits during described middle grinding and sieving device comprises, intermediate crusher, fine crusher, surge bunker, ore is by after front vibratory sieve in small, broken bits in described, ore in described on front Vibration Screen in small, broken bits is transported to described intermediate crusher and described fine crusher respectively by described belt feeder, in described under front Vibration Screen in small, broken bits, described intermediate crusher, described fine crusher is all connected with described surge bunker by described belt feeder, described surge bunker by described belt feeder be transported to described in front vibratory sieve in small, broken bits formed closed circuit,
Be connected with described lump ore ore deposit heap storage by described belt feeder in front Vibration Screen in small, broken bits in described; Also mix ore storage bin by described belt feeder and described fine ore under front Vibration Screen in small, broken bits in described to be connected.
6. ore reduction screening blending system according to claim 5, it is characterized in that, described coarse crushing device is jaw crusher.
7. ore reduction screening blending system according to claim 6, is characterized in that, is also provided with truck scale at described entrucking ore storage bin entrance and the outlet of described fine ore mixing ore storage bin; Described belt feeder is provided with belt conveyer scale.
8. ore reduction screening blending system according to claim 7, is characterized in that, be also provided with dust arrester in described crushing system and described screening system.
9. ore reduction screening blending system according to claim 8, it is characterized in that, described dust arrester is sack cleaner.
10. ore reduction screening blending system according to claim 9, is characterized in that, in described crushing system, described screening system and described blending system, be also provided with automatic inspection device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201520313364.5U CN204933628U (en) | 2015-05-15 | 2015-05-15 | A kind of ore reduction screening blending system |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109013077A (en) * | 2018-08-01 | 2018-12-18 | 中冶北方(大连)工程技术有限公司 | A kind of sorting process of earth's surface skarn type bloodstone |
CN113416837A (en) * | 2021-07-13 | 2021-09-21 | 中冶赛迪工程技术股份有限公司 | Ore is concentrated and is sieved blending system |
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2015
- 2015-05-15 CN CN201520313364.5U patent/CN204933628U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109013077A (en) * | 2018-08-01 | 2018-12-18 | 中冶北方(大连)工程技术有限公司 | A kind of sorting process of earth's surface skarn type bloodstone |
CN113416837A (en) * | 2021-07-13 | 2021-09-21 | 中冶赛迪工程技术股份有限公司 | Ore is concentrated and is sieved blending system |
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