CN107051691A - A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system - Google Patents
A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system Download PDFInfo
- Publication number
- CN107051691A CN107051691A CN201710228163.9A CN201710228163A CN107051691A CN 107051691 A CN107051691 A CN 107051691A CN 201710228163 A CN201710228163 A CN 201710228163A CN 107051691 A CN107051691 A CN 107051691A
- Authority
- CN
- China
- Prior art keywords
- gas
- finished product
- pulse dust
- inerting
- main frame
- 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.)
- Pending
Links
- 239000007789 gas Substances 0.000 claims abstract description 133
- 239000000428 dust Substances 0.000 claims abstract description 51
- 239000000463 material Substances 0.000 claims abstract description 44
- 238000004513 sizing Methods 0.000 claims abstract description 44
- 239000002994 raw material Substances 0.000 claims abstract description 31
- 239000000843 powder Substances 0.000 claims abstract description 30
- 238000004140 cleaning Methods 0.000 claims abstract description 25
- 238000007906 compression Methods 0.000 claims abstract description 20
- 230000006835 compression Effects 0.000 claims abstract description 20
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims abstract description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000002360 preparation method Methods 0.000 claims abstract description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000001301 oxygen Substances 0.000 claims abstract description 9
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 9
- 229910052786 argon Inorganic materials 0.000 claims abstract description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims description 10
- 238000001816 cooling Methods 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 6
- 230000008676 import Effects 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 238000009826 distribution Methods 0.000 abstract description 9
- 238000005516 engineering process Methods 0.000 abstract description 5
- 238000002485 combustion reaction Methods 0.000 abstract description 4
- 238000013473 artificial intelligence Methods 0.000 abstract description 3
- 238000001514 detection method Methods 0.000 abstract description 3
- 238000005457 optimization Methods 0.000 abstract description 3
- 239000002245 particle Substances 0.000 abstract description 3
- 239000000047 product Substances 0.000 description 52
- 238000012544 monitoring process Methods 0.000 description 13
- 108010066057 cabin-1 Proteins 0.000 description 7
- 238000004880 explosion Methods 0.000 description 5
- 238000000227 grinding Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 239000002360 explosive Substances 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000013022 venting Methods 0.000 description 2
- 241000208340 Araliaceae Species 0.000 description 1
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 1
- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- 210000001367 artery Anatomy 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000008542 thermal sensitivity Effects 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/04—Safety devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
- B02C23/20—Adding fluid, other than for crushing or disintegrating by fluid energy after crushing or disintegrating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C25/00—Control arrangements specially adapted for crushing or disintegrating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/06—Jet mills
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Disintegrating Or Milling (AREA)
Abstract
The present invention proposes a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system, the system uses argon gas or nitrogen for power gas source, including raw material cabin, crush main frame, gas flow sizing machine, cyclone separator, pulse dust collector, one-level finished product bin, two grades of finished product bins, inerting source of the gas preparation system, inerting gas is compressed and cleaning system and intelligent control module, raw material cabin, crush main frame, gas flow sizing machine, cyclone separator, pulse dust collector, cooperated between inerting source of the gas preparation system and inerting gas compression and cleaning system, and the circulatory system crushed with powder collection is formed by the control of intelligent control module.The present invention makes material completely cut off oxygen when being crushed in systems, with explosion-proof effect, big data and artificial intelligence technology and the identification Detection Techniques of material physicochemical character are employed, the technological parameter for carrying out most safe optimization for combustion is realized and automatically configures；Realize the controllable of superfine powder distribution and particle size range.
Description
Technical field
The present invention relates to lock air flow crushing device technical field, and in particular to a kind of intelligently realizing explosion-proof air-flow crushing and classification system
System.
Background technology
All kinds of Jet Mills that currently employed air flow principle is crushed are a lot, but present situation is：
First：Conventional air flow crushing device, can only crush conventional products, and to oxidizable, inflammable and explosive material, thermal sensitivity contains energy
Material is still difficult to crush, and safety can not be ensured, it is impossible to reach optimal anti-explosion safety；
Second：The existing inert gas shielding reducing mechanism part of in the market solves safety problem, but can only be directed to limited
Material crushed, can not be monitored and feed back in real time for some physicochemical characters of unfamiliar material in crushing process.
3rd：The setting of all technological parameters is required to artificial preset in advance, and once setting can not be adjusted voluntarily,
Specific aim for combustion is not strong, and adaptability of the physicochemical character to system running state of material can not be reflected in real time,
It is difficult to obtain optimal running status, is also just difficult to the superfine powder for obtaining optimal distribution state.
4th：Existing reducing mechanism can only obtain a kind of size distribution state and a kind of powder of fineness scope, it is impossible to same
When obtain several different smashing fineness, the superfine powder of different grain size distribution.
5th：The intelligence degree of control is relatively low, only carries out static monitoring to the running status of system in itself, it is impossible to be directed to
Material condition carries out the dynamic regulation of dynamic monitoring and running status.
Therefore, in view of the above-mentioned problems, the present invention proposes a kind of new technical scheme.
The content of the invention
In order to overcome drawbacks described above, the invention provides one kind using argon gas or nitrogen be the ultra-fine grinding of power gas source collection with point
Level relies on big data and artificial intelligence technology in the intelligently realizing explosion-proof air-flow crushing and hierarchy system of one, the system, can be according to thing
Expect the real-time trend adjustment system running state of physicochemical character, and different grain size distribution and different fineness scope can be obtained simultaneously
Superfine powder.
The present invention is achieved through the following technical solutions：
A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system, the system use argon gas or nitrogen for power gas source, including raw material cabin,
Crush main frame, gas flow sizing machine, cyclone separator, pulse dust collector, one-level finished product bin, two grades of finished product bins, inerting sources of the gas
Preparation system, inerting gas compression and cleaning system and intelligent control module, the material outlet of the raw material cabin lower end and crushing
Material inlet on main frame is communicated, and the material outlet morcelled on main frame is communicated with the material inlet on gas flow sizing machine, institute
The gas stated on gas flow sizing machine is communicated with fine powder outlet with the material inlet on cyclone separator, on the cyclone separator
Gas vent is communicated with the air inlet on pulse dust collector, the compression of the gas vent on the pulse dust collector and inerting gas with
The air inlet of cleaning system is communicated, and the inerting gas compression is with the gas vent in cleaning system with expecting the air inlet on broken main frame
Mouth is communicated, and the gas vent of the inerting source of the gas preparation system is communicated with inerting gas compression with the air inlet of cleaning system, institute
State raw material cabin, crush main frame, gas flow sizing machine, cyclone separator, pulse dust collector, inerting source of the gas preparation system and inerting gas
Cooperated between compression and cleaning system, and the cyclic system that crushing is collected with powder is formed by the control of intelligent control module
System；
The gas flow sizing machine lower end is exported provided with coarse powder, the charging aperture phase of the coarse powder outlet and two grades of finished product bin top
Logical, the material outlet on the cyclone separator is communicated with the first charging aperture of one-level finished product bin upper end, the pulse dust removal
Material outlet on device is communicated with the second charging aperture of one-level finished product bin upper end, the one-level finished product bin and two grades of finished product materials
Charging basket is collected with the finished product that inerting gas is protected and is connected in storehouse；
Described crush is equipped with on-line sampler on the pipeline that main frame discharging opening is communicated with the material inlet on gas flow sizing machine, described
Gas flow sizing machine, cyclone separator and pulse dust collector lower end, which are equipped with transitional storehouse, transitional storehouse, is mounted on on-line sampler；
The raw material cabin, one-level finished product bin, two grades of finished product bins, crush in main frame and pulse dust collectors and be respectively arranged with oxygen concentration
Sensor.
Further, the inerting gas compression includes air compressor machine, oil expeller, cooling driers and at least two with cleaning system
Accurate filter, the cooling driers both sides are equipped with accurate filter, and side accurate filter is with crushing the air inlet on main frame
It is connected, opposite side accurate filter is connected with oil expeller, the oil expeller is connected with air compressor machine, the air compressor machine and arteries and veins
The gas vent rushed on deduster is connected.
Further, the raw material cabin, crushing main frame, gas flow sizing machine, cyclone separator, pulse dust collector and inerting gas
Body compresses constitutes a closed-circuit system with cleaning system.
Further, the gas flow sizing machine, cyclone separator, pulse dust collector, one-level finished product bin and two grades of finished products
Feed bin discharge method is discharged with pneumatic ball valve with star outlet valve lock gas.
Further, on the raw material cabin, crushing main frame, gas flow sizing machine, one-level finished product bin and two grades of finished product bins
Temperature sensor and pressure sensor are mounted on, the cyclone separator and pulse dust collector are provided with temperature sensor.
Further, the raw material cabin, gas flow sizing machine, cyclone separator, pulse dust collector, one-level finished product bin and two
Relief valve is equipped with level finished product bin.
Further, differential pressure pickup is provided with the pulse dust collector.
The beneficial effects of the invention are as follows：It is power gas source present invention employs argon gas or nitrogen, material is entered in systems
Row has completely cut off oxygen when crushing, and the explosion-proof of Jet Crushing is become possibility, while employing big data and artificial intelligence
The identification Detection Techniques of technology and material physicochemical character, realize the technique ginseng that most safe optimization is carried out for combustion
Number is automatically configured；And add gas flow sizing machine so that in a crushing system can simultaneously or different distributions state and
The superfine powder of different-grain diameter scope, realizes the controllable of superfine powder distribution and particle size range.
Brief description of the drawings
Fig. 1 is structural representation of the invention；
Fig. 2 is raw material cabin and the structural representation for crushing main frame；
Fig. 3 is the structural representation of gas flow sizing machine；
Fig. 4 is the structural representation of cyclone separator；
Fig. 5 is the structural representation of pulse dust collector；
Fig. 6 is the structural representation of one-level finished product bin；
Fig. 7 is the structural representation of two grades of finished product bins；
Fig. 8 is inerting gas compression and the structural representation of cleaning system.
Wherein：1st, raw material cabin, 2, crush main frame, 3, gas flow sizing machine, 4, cyclone separator, 5, pulse dust collector, 6, one
Level finished product bin, 7, two grades of finished product bins, 8, inerting source of the gas preparation system, 9, inerting gas compression and cleaning system, 10, intelligence
Control system, 11, gas and fine powder export, 12, coarse powder outlet, 13, first charging aperture, the 14, second material material mouth, 15, charging aperture,
16th, oil expeller, 17, accurate filter, 18, cooling driers, 19, air compressor machine, 21, transitional storehouse, 22, star-like outlet valve, 23, Pneumatic ball
Valve, 24, on-line sampler, 101, relief valve, 201, temperature sensor, 202, pressure sensor, 301, oxygen concentration sensor,
401st, differential pressure pickup.
Embodiment
Illustrate to be described further invention below in conjunction with the accompanying drawings.
As shown in Fig. 1 ~ 8, a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system, the system use argon gas or nitrogen for power
Source of the gas, including raw material cabin 1, crush main frame 2, gas flow sizing machine 3, cyclone separator 4, pulse dust collector 5, one-level finished product bin 6,
Two grades of finished product bins 7, inerting source of the gas preparation system 8, inerting gas are compressed and cleaning system 9 and intelligent control module 10, raw material
The material outlet of the lower end of storehouse 1 is communicated with crushing the material inlet on main frame 2, morcels the material outlet and air current classifying on main frame 2
Material inlet on machine 3 is communicated, and the gas on gas flow sizing machine 3 exports 11 and the material inlet on cyclone separator 4 with fine powder
Communicate, the gas vent on cyclone separator 4 is communicated with the air inlet on pulse dust collector 5, the gas on pulse dust collector 5 goes out
Mouthful with inerting gas compression is communicated with the air inlet of cleaning system 9, inerting gas compression and cleaning system 9 on gas vent and
Expect that the air inlet on broken main frame 2 is communicated, gas vent and the inerting gas compression and cleaning system 9 of inerting source of the gas preparation system 8
Air inlet communicate, raw material cabin 1, crush main frame 2, gas flow sizing machine 3, cyclone separator 4, pulse dust collector 5, inerting source of the gas system
Cooperated between standby system 8 and inerting gas compression and cleaning system 9, and powder is formed by the control of intelligent control module 10
The broken circulatory system collected with powder；
The lower end of gas flow sizing machine 3 is provided with coarse powder outlet 12, the phase of charging aperture 15 of coarse powder outlet 12 and two grades of top of finished product bin 7
Logical, the material outlet on cyclone separator 4 is communicated with the first charging aperture 13 of the upper end of one-level finished product bin 6, on pulse dust collector 5
Material outlet communicated with the second charging aperture 14 of the upper end of one-level finished product bin 6, one-level finished product bin 6 and two grades of finished product bins 7
Charging basket is collected with the finished product that inerting gas is protected to be connected；
Crush and on-line sampler 24, air-flow are housed on the pipeline that the discharging opening of main frame 2 is communicated with the material inlet on gas flow sizing machine 3
Grader 3, cyclone separator 4 and the lower end of pulse dust collector 5, which are equipped with transitional storehouse 21, transitional storehouse 21, is mounted on on-line period
Device 24；
Raw material cabin 1, one-level finished product bin 6, two grades of finished product bins 7, crush that to be respectively arranged with oxygen in main frame 2 and pulse dust collectors 5 dense
Spend sensor 301.
In the present embodiment, inerting gas compression includes air compressor machine 19, oil expeller 16, cooling driers 18 and extremely with cleaning system 9
Few two accurate filters 17, the both sides of cooling driers 18 are equipped with accurate filter 17, and side accurate filter 17 is with crushing main frame 3
On air inlet be connected, opposite side accurate filter 17 is connected with oil expeller 16, and oil expeller 16 is connected with air compressor machine 19,
Air compressor machine 19 is connected with the gas vent on pulse dust collector 5.
In the present embodiment, raw material cabin 1, crushing main frame 2, gas flow sizing machine 3, cyclone separator 4, the and of pulse dust collector 5
Inerting gas is compressed constitutes a closed-circuit system with cleaning system 9.Raw material cabin 1, one-level finished product bin 6 and two grades of finished product bins 7
Protected using inerting gas.
In the present embodiment, gas flow sizing machine 3, cyclone separator 4, pulse dust collector 5, one-level finished product bin 6 and two grades
The discharge method of finished product bin 7 is discharged with pneumatic ball valve 23 with the lock gas of star outlet valve 22.Realize the blast between process equipment
Isolation and system and operating area isolate.
In the present embodiment, raw material cabin 1, crushing main frame 2, gas flow sizing machine 3, one-level finished product bin 6 and two grades of finished product materials
Temperature sensor 201 and pressure sensor 202 are mounted on storehouse 7, cyclone separator 4 and pulse dust collector 5 are provided with temperature
Sensor 201.
In the present embodiment, raw material cabin 1, gas flow sizing machine 3, cyclone separator 4, pulse dust collector 5, one-level finished product bin
6 and two grades of finished product bins 7 on be equipped with relief valve 101.The installation site of the system is used lets out without flame pressure relief device or use
Pressure relief opening is led to outdoor by pressure conduit.
In the present embodiment, differential pressure pickup 401 is provided with pulse dust collector 5.
In the present embodiment, main frame 2, cyclone separator 4, transitional storehouse 21 are crushed and uses anti-explosion design, crush main frame 2
Material outlet is communicated with the charging aperture of gas flow sizing machine 3, and real-time graded is carried out to the material after crushing；Meanwhile, pneumatic ball valve 23
Set location Sensor monitoring on off state, star-like outlet valve 22 sets noncontact proximity switch monitoring rotating speed.Realize oxygen dense
" anti-explosion safety " the intelligent control logics such as degree is automatically controlled, monitoring-temperature alarm, crushing Stress control, autompulse deashing, and
And, monitored in real time using powder granularity, and realize that energy-saving " performance optimization " intelligent control is patrolled by technological parameter regulation and control
Volume.
The operation principle of the system is：The present invention collects ultra-fine grinding and is classified in one using argon gas or nitrogen as power gas source
The intelligently realizing explosion-proof air-flow crushing and hierarchy system of body, the high pressure inerting gas for being pressurized to 0.8 ~ 1.0Mpa through compressor, which enters, to be crushed
Main frame, the raw material cabin that raw material is protected via inerting gas enters crushing main frame and crushed.Powder after crushing is carried in air-flow
Lower entrance gas flow sizing machine, the material after crushing is classified on demand.Fine powder after classification enters cyclonic separation with air-flow
Device carries out finished product collection, by again by inerting gas positive pneumatic transport to one-level finished product bin（Superfine powder feed bin）.Cyclonic separation
The inerting gas that device outlet carries a small amount of dust returns to compressor inlet after pulse dust collector and secondary filter purification.Gas
Powder relatively thick enters to two grades of finished product bins through inerting gas positive-pressure pneumatic after current classifier classification（Fine powder feed bin）.
Gas flow sizing machine, cyclone separator, pulse dust collector, one-level finished product bin and two grades of finished product bins discharging opening it is equal
For pneumatic ball valve+star-like outlet valve.Pneumatic ball valve has an excellent sealing, and star-like outlet valve can be realized even under the conditions of lock gas
Fast blanking.Pneumatic ball valve is opened when different with rotating blanking valve, can be achieved between process equipment, process equipment and Work places
Blast isolation.In raw material cabin, gas flow sizing machine, pulse dust collector, finished product bin, pressure relief opening is set.According to the installation position of the system
Put and lead to outdoor using without flame pressure relief device or using venting conduit by pressure relief opening.Crush main frame and cyclone separator, excessively
Storehouse and conveying storehouse use anti-explosion design.
Main frame is being crushed to gas flow sizing machine, gas flow sizing machine to cyclone separator, gas flow sizing machine to two grades of finished product materials
On-line period mouthful is mounted on the pipeline in storehouse, to carry out real-time or off-line monitoring to raw meal particle size distribution.
In the entrance of the outlet of pulse dust collector and airslide disintegrating mill, raw material cabin and one-level finished product bin and two grades of finished product materials
Storehouse sets oxygen concentration sensor.Crush main frame, gas flow sizing machine, cyclone separator, pulse dust collector, one-level finished product bin and
Temperature sensor is set in two grades of finished product bins.Raw material cabin, crush main frame inlet duct, gas flow sizing machine, pulse dust collector,
One-level finished product bin, two grades of finished product bins and air accumulator（Air accumulator is located at inerting source of the gas preparation system）Pressure sensor is set.
Differential pressure pickup is set between the dirty room of pulse dust collector and clean room.Pneumatic ball valve set location Sensor monitoring on off state,
Star-like outlet valve sets noncontact proximity switch monitoring rotating speed.
Total system uses intelligentized control method：Be not in igniting during by realizing normal operation with control to oxygen concentration monitoring
Source.Spontaneous combustion early signal can be found by temperature monitoring, in time supplement inerting gas or maintenance down.Entered by airslide disintegrating mill
The monitoring of mouth pipeline pressure and the controllable crushing air flow rate of control, and then control to crush production capacity.The monitoring of deduster pressure difference can be used for
Cloth bag dust-removing control, while cloth bag perforation can be found in time or the failure situations such as imprecision are installed.Pneumatic ball valve and lock gas discharging
Unit state monitors the normal operation that can ensure that whole system., can automatic monitoring system in the case of hookup wire granularity Detection
Energy consumption and Granularity Distribution, and by adjusting feed rate and crushing gas pressure Optimizing Process Parameters.
The monitoring of the system integrated use technological parameter, inerting, flame proof, venting of dust explosion and aniknock technology, realize inflammable and explosive powder
The safe ultra-fine grinding of body.
Claims (7)
1. a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system, the system use argon gas or nitrogen for power gas source, including raw material
Storehouse, crushing main frame, gas flow sizing machine, cyclone separator, pulse dust collector, one-level finished product bin, two grades of finished product bins, inerting gas
Source preparation system, inerting gas compression and cleaning system and intelligent control module, it is characterised in that：The thing of the raw material cabin lower end
Material outlet is communicated with crushing the material inlet on main frame, the material on the material outlet and gas flow sizing machine crushed on main frame
Import is communicated, and the gas on the gas flow sizing machine is communicated with fine powder outlet with the material inlet on cyclone separator, the rotation
Gas vent on wind separator is communicated with the air inlet on pulse dust collector, the gas vent on the pulse dust collector with it is lazy
Change gas compression to communicate with the air inlet of cleaning system, the inerting gas compression is with the gas vent in cleaning system with expecting broken
Air inlet on main frame is communicated, gas vent and the inerting gas compression of the inerting source of the gas preparation system and entering for cleaning system
Gas port is communicated, and the raw material cabin, crushing main frame, gas flow sizing machine, cyclone separator, pulse dust collector, inerting source of the gas prepare system
Cooperated between system and inerting gas compression and cleaning system, and crushing and powder are formed by the control of intelligent control module
The circulatory system of collection；
The gas flow sizing machine lower end is exported provided with coarse powder, the charging aperture phase of the coarse powder outlet and two grades of finished product bin top
Logical, the material outlet on the cyclone separator is communicated with the first charging aperture of one-level finished product bin upper end, the pulse dust removal
Material outlet on device is communicated with the second charging aperture of one-level finished product bin upper end, the one-level finished product bin and two grades of finished product materials
Charging basket is collected with the finished product that inerting gas is protected and is connected in storehouse；
Described crush is equipped with on-line sampler on the pipeline that main frame discharging opening is communicated with the material inlet on gas flow sizing machine, described
Gas flow sizing machine, cyclone separator and pulse dust collector lower end, which are equipped with transitional storehouse, transitional storehouse, is mounted on on-line sampler；
The raw material cabin, one-level finished product bin, two grades of finished product bins, crush in main frame and pulse dust collectors and be respectively arranged with oxygen concentration
Sensor.
2. a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system according to claim 1, it is characterised in that：The inerting gas
Body compresses includes air compressor machine, oil expeller, cooling driers and at least two accurate filters with cleaning system, and the cooling driers both sides are equal
Provided with accurate filter, side accurate filter is connected with crushing the air inlet on main frame, and opposite side accurate filter is with removing
Oily device is connected, and the oil expeller is connected with air compressor machine, and the air compressor machine is connected with the gas vent on pulse dust collector.
3. a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system according to claim 1, it is characterised in that：The raw material cabin,
Crush main frame, gas flow sizing machine, cyclone separator, pulse dust collector and inerting gas compression and cleaning system composition one is closed circuit
System.
4. a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system according to claim 1, it is characterised in that：The air current classifying
Machine, cyclone separator, pulse dust collector, one-level finished product bin and two grades of finished product bin discharge methods use pneumatic ball valve and star
Outlet valve lock gas discharging.
5. a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system according to claim 1, it is characterised in that：The raw material cabin,
Crush and be mounted on temperature sensor and pressure sensing on main frame, gas flow sizing machine, one-level finished product bin and two grades of finished product bins
Device, the cyclone separator and pulse dust collector are provided with temperature sensor.
6. a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system according to claim 1, it is characterised in that：The raw material cabin,
Relief valve is equipped with gas flow sizing machine, cyclone separator, pulse dust collector, one-level finished product bin and two grades of finished product bins.
7. a kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system according to claim 1, it is characterised in that：The pulse dust removal
Differential pressure pickup is provided with device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710228163.9A CN107051691A (en) | 2017-04-10 | 2017-04-10 | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710228163.9A CN107051691A (en) | 2017-04-10 | 2017-04-10 | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107051691A true CN107051691A (en) | 2017-08-18 |
Family
ID=59601753
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710228163.9A Pending CN107051691A (en) | 2017-04-10 | 2017-04-10 | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107051691A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108271594A (en) * | 2018-03-26 | 2018-07-13 | 南京林业大学 | A kind of bamboo grove rice chaff collection method and its modularization collection device |
| CN109292462A (en) * | 2018-10-12 | 2019-02-01 | 吉林市新大科机电技术有限责任公司 | A kind of twin-stage gas-solid separating device for air-transport system |
| CN109331984A (en) * | 2017-09-12 | 2019-02-15 | 上海美矿机械有限公司 | A kind of ball mill expert intelligence configuration cloud control system and control method |
| CN109954554A (en) * | 2017-12-25 | 2019-07-02 | 江苏天元金属粉末有限公司 | The high activity superfine spherical aluminium powder and its hierarchy system of controllable oxidization shell |
| CN111855249A (en) * | 2020-07-29 | 2020-10-30 | 四川皇龙智能破碎技术股份有限公司 | Powder preparation system test method |
| CN111879541A (en) * | 2020-07-29 | 2020-11-03 | 四川皇龙智能破碎技术股份有限公司 | Powder preparation system test platform |
| CN112138828A (en) * | 2020-07-27 | 2020-12-29 | 营口航盛科技实业有限责任公司 | Superfine grinding device system of battery-grade lithium hydroxide |
| CN113262585A (en) * | 2021-05-28 | 2021-08-17 | 广东金方圆安全技术检测有限公司 | Explosion suppression control system of laser welding dust remover |
| CN116078510A (en) * | 2022-11-23 | 2023-05-09 | 苏州金远胜智能装备股份有限公司 | Explosion-proof jet milling system and control method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1559694A (en) * | 2004-03-05 | 2005-01-05 | 昆山密友实业有限公司 | Ultra micro air flow pulverizer set with inert gas shielded |
| CN101116840A (en) * | 2006-08-01 | 2008-02-06 | 昆山密友实业有限公司 | Inert gas protection and on-line detecting ultra-fine comminuting system |
| CN105363541A (en) * | 2015-11-28 | 2016-03-02 | 南阳福森镁粉有限公司 | Magnesium metal smashing and grading device and technique thereof |
| CN105944816A (en) * | 2016-06-21 | 2016-09-21 | 江苏密友粉体新装备制造有限公司 | Safe explosion-proof airflow pulverization system |
| CN206701447U (en) * | 2017-04-10 | 2017-12-05 | 太仓金溪粉碎设备有限公司 | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system |
-
2017
- 2017-04-10 CN CN201710228163.9A patent/CN107051691A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1559694A (en) * | 2004-03-05 | 2005-01-05 | 昆山密友实业有限公司 | Ultra micro air flow pulverizer set with inert gas shielded |
| CN101116840A (en) * | 2006-08-01 | 2008-02-06 | 昆山密友实业有限公司 | Inert gas protection and on-line detecting ultra-fine comminuting system |
| CN105363541A (en) * | 2015-11-28 | 2016-03-02 | 南阳福森镁粉有限公司 | Magnesium metal smashing and grading device and technique thereof |
| CN105944816A (en) * | 2016-06-21 | 2016-09-21 | 江苏密友粉体新装备制造有限公司 | Safe explosion-proof airflow pulverization system |
| CN206701447U (en) * | 2017-04-10 | 2017-12-05 | 太仓金溪粉碎设备有限公司 | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109331984A (en) * | 2017-09-12 | 2019-02-15 | 上海美矿机械有限公司 | A kind of ball mill expert intelligence configuration cloud control system and control method |
| CN109331984B (en) * | 2017-09-12 | 2020-10-30 | 上海美矿机械股份有限公司 | Expert intelligent configuration cloud control system and control method for ball mill |
| CN109954554A (en) * | 2017-12-25 | 2019-07-02 | 江苏天元金属粉末有限公司 | The high activity superfine spherical aluminium powder and its hierarchy system of controllable oxidization shell |
| CN109954554B (en) * | 2017-12-25 | 2024-05-28 | 江苏天元金属粉末有限公司 | High-activity superfine spherical aluminum powder with controllable oxide shell layer and grading system thereof |
| CN108271594A (en) * | 2018-03-26 | 2018-07-13 | 南京林业大学 | A kind of bamboo grove rice chaff collection method and its modularization collection device |
| CN109292462B (en) * | 2018-10-12 | 2023-12-15 | 吉林市新大科机电技术有限责任公司 | Double-stage gas-solid separation device for pneumatic conveying system |
| CN109292462A (en) * | 2018-10-12 | 2019-02-01 | 吉林市新大科机电技术有限责任公司 | A kind of twin-stage gas-solid separating device for air-transport system |
| CN112138828A (en) * | 2020-07-27 | 2020-12-29 | 营口航盛科技实业有限责任公司 | Superfine grinding device system of battery-grade lithium hydroxide |
| CN111879541A (en) * | 2020-07-29 | 2020-11-03 | 四川皇龙智能破碎技术股份有限公司 | Powder preparation system test platform |
| CN111855249A (en) * | 2020-07-29 | 2020-10-30 | 四川皇龙智能破碎技术股份有限公司 | Powder preparation system test method |
| CN113262585B (en) * | 2021-05-28 | 2022-07-19 | 广东金方圆安全技术检测有限公司 | Explosion suppression control system of laser welding dust remover |
| CN113262585A (en) * | 2021-05-28 | 2021-08-17 | 广东金方圆安全技术检测有限公司 | Explosion suppression control system of laser welding dust remover |
| CN116078510A (en) * | 2022-11-23 | 2023-05-09 | 苏州金远胜智能装备股份有限公司 | Explosion-proof jet milling system and control method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107051691A (en) | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system | |
| CN106269803B (en) | A kind of waste refrigerators harmless disassembly and resource classification reclaimer and method | |
| CN206701447U (en) | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system | |
| CN103537355B (en) | System and method for preparing ultrafine pulverized coal | |
| CN206296295U (en) | A kind of waste refrigerators harmless disassembly and resource classification reclaimer | |
| CN204503371U (en) | With the air-flow vortex flour mill that deduster duplex is gathered materials | |
| CN206276485U (en) | A kind of micronizer | |
| CN110600757A (en) | Lithium battery negative electrode material component extraction production line | |
| CN1259235C (en) | Processing technology and system for high-purity fine crystalline graphite powder | |
| CN218250708U (en) | Grinding system | |
| CN202316310U (en) | Horizontal airflow classifier | |
| CN105772197B (en) | A kind of ultra tiny roller mill equipment production flow | |
| CN205684173U (en) | A kind of automatic high energy categorizing system of carborundum | |
| CN212328572U (en) | Smash wearing sieve monitoring devices of in-process automatic sampling | |
| CN113455203A (en) | Multifunctional straw biomass crushing system and crushing method | |
| CN203525457U (en) | Pulse funnel-type dust collecting plant for carbon dust manufacturing shop | |
| CN112935269A (en) | Plasma powder making device with grading device and powder making process thereof | |
| CN201632177U (en) | All-in-one dedusting separation machine | |
| CN208260957U (en) | Feed Manufacturing is classified wind with crushing material and send cooling system | |
| JPH04135654A (en) | Grinder | |
| CN209061335U (en) | Wet face head recovery system | |
| CN202427526U (en) | Fine smashing system | |
| CN106378236A (en) | Vertical grinding machine for glass fiber | |
| CN202845328U (en) | Multifunctional rotary screen | |
| CN208321033U (en) | A kind of white cement processing unit (plant) with ash removing mechanism |
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 | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170818 |