CN106179787B - Graphite crushes and nodularization system - Google Patents
Graphite crushes and nodularization system Download PDFInfo
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- CN106179787B CN106179787B CN201610547694.XA CN201610547694A CN106179787B CN 106179787 B CN106179787 B CN 106179787B CN 201610547694 A CN201610547694 A CN 201610547694A CN 106179787 B CN106179787 B CN 106179787B
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 229910002804 graphite Inorganic materials 0.000 title claims abstract description 33
- 239000010439 graphite Substances 0.000 title claims abstract description 33
- 238000007493 shaping process Methods 0.000 claims abstract description 93
- 239000000463 material Substances 0.000 claims abstract description 46
- 239000002699 waste material Substances 0.000 claims abstract description 32
- 238000005303 weighing Methods 0.000 claims abstract description 29
- 230000003139 buffering effect Effects 0.000 claims abstract description 5
- 238000004519 manufacturing process Methods 0.000 description 10
- 239000002245 particle Substances 0.000 description 9
- 239000000843 powder Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 230000009191 jumping Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000012549 training Methods 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 235000012550 Pimpinella anisum Nutrition 0.000 description 1
- 240000004760 Pimpinella anisum Species 0.000 description 1
- 241000555745 Sciuridae Species 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910021389 graphene Inorganic materials 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000005563 spheronization Methods 0.000 description 1
- 230000002123 temporal effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
Abstract
The present invention provides a kind of graphite crushing and nodularization system, including：Sequentially connected feed hopper, jet microniser, whirlwind clarifier, shaping feed bin sum aggregate material unit；Wherein, collection material unit includes：Shaping feed bin is connected with weighing silo, feed inlet of the weighing silo also with shaping grader is connected, the discharge port of the plastic section of shaping grader is connected with the feed inlet of finished bin, the discharge port of the classification section of shaping grader is connected with the feed inlet in waste product storehouse, finished bin is connected with waste product storehouse, and finished bin and waste product storehouse are connected respectively with a buffering bucket；Waste product storehouse and shaping feed bin are connected respectively with first air-introduced machine, and jet microniser is also connected with air blower.Pass through above system, material is successively by the crushing of jet microniser and the shaping of shaping grader, so as to material is crushed and nodularization during, without increase crush and shaping number so that graphite crush and nodularization system output increased within the unit interval.
Description
Technical field
The present invention relates to micro mist crushing and spheronization techniques more particularly to a kind of graphite crushes and nodularization system.
Background technology
Graphite is known as the laudatory title of " dark fund ", in addition to can be used for the high-grade, precision and advanced technical field such as lithium battery, display screen,
The fields such as defence and military, energy conservation and environmental protection purposes is wide.By environmental protection and new material factors influencing demand, graphite industry is in graphene, artificial
The concerned degree of the sub-industries such as diamond is increasing.New material, the particle size range of new energy requirement graphite microparticles particle are narrow, spherical
Degree is high, tap density is big therefore very high to the equipment requirement of machining graphite.
The common grinding modes such as air-flow crushing or vibro-grinding processing graphite at present, product is typically rubble shape structure,
Grain size is uneven, and in irregular shape, corner angle are sharp, needs through multiple low speed, crushes at a high speed and be polished to spheric granules.
The prior art often, leads to low output in single set system unit time due to crushing, shaping.
Invention content
The embodiment of the present invention provides a kind of graphite crushing and nodularization system, to overcome in the prior art due to crushing, shaping
Often, lead to single the problem of covering low output in the system unit time.
The embodiment of the present invention provides a kind of graphite crushing and nodularization system, including：Sequentially connected feed hopper, jet mill
Machine, whirlwind clarifier, shaping feed bin sum aggregate material unit；
The collection material unit includes：Weighing silo, shaping grader, finished bin and waste product storehouse, the shaping feed bin and institute
Weighing silo is stated to be connected, feed inlet of the weighing silo also with the shaping grader is connected, the shaping grader it is whole
The discharge port of shape section is connected with the feed inlet of the finished bin, discharge port and the waste product of the classification section of the shaping grader
The feed inlet in storehouse is connected, and the finished bin is connected with the waste product storehouse, and the finished bin and the waste product storehouse are slow with one respectively
Punching bucket is connected；
The waste product storehouse and the shaping feed bin are connected respectively with first air-introduced machine, the jet microniser also with drum
Wind turbine is connected.
Optionally, the system also includes：Squirrel-cage crusher,
The squirrel-cage crusher is connected by the feed hopper with the jet microniser.
Optionally, the feed hopper includes：Big hopper and small hopper；
The squirrel-cage crusher is connected with the big hopper, and the big hopper is connected with the small hopper, the small powder
Bucket is connected with the jet microniser.
Optionally, the system also includes：First screw conveyor and the second screw conveyor,
The small hopper is connected with the jet microniser, including：The small hopper passes through first conveyer and institute
Jet microniser is stated to be connected；
Feed inlet of the weighing silo also with the shaping grader is connected, including：The weighing silo passes through described
Second conveyor is connected with the feed inlet of the shaping grader.
Optionally, the system also includes：First star-shaped feeding machine and the second star-shaped feeding machine；
The big hopper is connected with the small hopper, including：The big hopper passes through first star-shaped feeding machine and institute
Small hopper is stated to be connected；
The shaping feed bin is connected with the weighing silo, including：The shaping feed bin passes through the described second star-like feed
Machine is connected with the weighing silo.
Optionally, the system also includes：Pulverizer collecting bin；
The whirlwind clarifier is connected with the shaping feed bin, including：The whirlwind clarifier is received by the pulverizer
Ji Cang is connect with the shaping feed bin；
The pulverizer collecting bin is also connected with second air-introduced machine.
Optionally, the inside of the pulverizer collecting bin, the inside of the shaping feed bin, the inside in the waste product storehouse, institute
The inside for stating finished bin sets at least one dedusting filtering bag respectively.
Optionally, the shaping feed bin includes at least one cone, collects material unit described in each one group of cone connection.
Optionally, first conveyer is：First screw conveyor or the first oscillating feeder；
The second conveyor is：Second screw conveyor or the second oscillating feeder；
Optionally, if the second conveyor is the second screw conveyor, the cylinder of second screw conveyor passes through
Flange is directly connected with the shaping grader pipe connecting flange, and the tubular axis of second screw conveyor and the shaping
Angle between grader tubular axis is less than or equal to 90 ° and more than or equal to 30 °.
Graphite provided in this embodiment crushes and nodularization system, including：Sequentially connected feed hopper, jet microniser, rotation
Wind grader, shaping feed bin sum aggregate material unit；Wherein, collection material unit includes：Weighing silo, shaping grader, finished bin and useless
Product storehouse, shaping feed bin are connected with weighing silo, and feed inlet of the weighing silo also with shaping grader is connected, shaping grader it is whole
The discharge port of shape section is connected with the feed inlet of finished bin, the discharge port of the classification section of shaping grader and the feed inlet phase in waste product storehouse
Even, finished bin is connected with waste product storehouse, and finished bin and waste product storehouse are connected respectively with a buffering bucket；Waste product storehouse and shaping feed bin difference
It is connected with first air-introduced machine, jet microniser is also connected with air blower.By above system, material passes through jet stream powder successively
The crushing of broken machine and the shaping of shaping grader, so as to material is crushed and nodularization during, without increase crush
With the number of shaping so that graphite crush and nodularization system output increased within the unit interval.
Description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, to embodiment or will show below
There is attached drawing needed in technology description to be briefly described, it should be apparent that, the accompanying drawings in the following description is this hair
Some bright embodiments, for those of ordinary skill in the art, without having to pay creative labor, can be with
Other attached drawings are obtained according to these attached drawings.
Fig. 1 show the structure diagram one of graphite crushing provided in an embodiment of the present invention and nodularization system；
Fig. 2 show the structure diagram two of graphite crushing provided in an embodiment of the present invention and nodularization system.
Specific embodiment
Below in conjunction with the attached drawing in the embodiment of the present invention, the technical solution in the embodiment of the present invention is carried out clear, complete
Site preparation describe, it is clear that described embodiment be only part of the embodiment of the present invention, the embodiment being not all of.Based on this
Embodiment in invention, the every other reality that those of ordinary skill in the art are obtained without making creative work
Example is applied, shall fall within the protection scope of the present invention.
Specification, claims and the term " first " in above-mentioned attached drawing of the present invention, " second " etc. are for distinguishing
Similar object rather than for describing specific sequence or precedence.In addition, term " comprising " and " having " and they
Any deformation, it is intended that cover it is non-exclusive include, for example, containing the process of series of steps, method, comprising a system
Column unit, the system of module, product or equipment are not necessarily limited to those steps or unit clearly listed, but may include not having
It is clearly listing or for the intrinsic other steps of these processes, method, product or equipment or unit.It is involved in the present invention
" at least one " refer to one kind or a variety of meanings.
Due to crushing, shaping often, causing powder inside, there are a large amount of nanoscale and Subnano-class for the prior art
Graphite differential, lead to that Granularity Distribution range is wide, and sphericity is low, tap density is low, and yield rate only has 50% or so；Its
It is secondary, increase due to crushing with shaping number, power consumption is caused to increase, production cost greatly improves；In addition, since the prior art crushes
And training time is long, leads to low output in single set system unit time.
The present invention crushes jet microniser and shaping grader by setting, so that material needs not move through multiple crushing
And shaping, power consumption and production cost are effectively reduced, and improve yield in the system unit time.
Purpose, technical scheme and advantage to make the embodiment of the present invention are clearer, below in conjunction with the embodiment of the present invention
In attached drawing, the technical solution in the embodiment of the present invention is described.
Fig. 1 show the structure diagram one of graphite crushing provided in an embodiment of the present invention and nodularization system, such as Fig. 1 institutes
Show, graphite provided in this embodiment crushes and nodularization system can include：
Sequentially connected feed hopper 1, jet microniser 2, whirlwind clarifier 3,4 sum aggregate material unit 5 of shaping feed bin；
Collection material unit 5 includes：Weighing silo 51, shaping grader 52, finished bin 53 and waste product storehouse 54, shaping feed bin 4 with
Weighing silo 51 is connected, and feed inlet of the weighing silo 51 also with shaping grader 52 is connected, the plastic section of shaping grader 52
Discharge port is connected with the feed inlet of finished bin 53, the discharge port of the classification section of shaping grader 52 and the feed inlet phase in waste product storehouse 54
Even, finished bin 53 is connected with waste product storehouse 54, and finished bin 53 and waste product storehouse 54 are connected respectively with a buffering bucket 55；
Waste product storehouse 54 and shaping feed bin 4 are connected respectively with first air-introduced machine 6, jet microniser 2 also with 7 phase of air blower
Even.
Graphite provided in this embodiment crushes and nodularization system, including：Sequentially connected feed hopper, jet microniser, rotation
Wind grader, shaping feed bin sum aggregate material unit；Wherein, collection material unit includes：Weighing silo, shaping grader, finished bin and useless
Product storehouse, shaping feed bin are connected with weighing silo, and feed inlet of the weighing silo also with shaping grader is connected, shaping grader it is whole
The discharge port of shape section is connected with the feed inlet of finished bin, the discharge port of the classification section of shaping grader and the feed inlet phase in waste product storehouse
Even, finished bin is connected with waste product storehouse, and finished bin and waste product storehouse are connected respectively with a buffering bucket；Waste product storehouse and shaping feed bin difference
It is connected with first air-introduced machine, jet microniser is also connected with air blower.By above system, material passes through jet stream powder successively
The crushing of broken machine and the shaping of shaping grader, so as to material is crushed and nodularization during, without increase crush
With the number of shaping so that graphite crush and nodularization system output increased within the unit interval.
If the material particles into system are smaller in itself, powder is carried out so as to be directly entered jet microniser
It is broken, it is just broken with regard to needing to carry out at this time but if the material particles itself into system are bigger, be by the crushing material of bulky grain
The material of smaller particle, and then into jet microniser so that jet microniser crush it is just easy.
Fig. 2 show the structure diagram two of graphite crushing provided in an embodiment of the present invention and nodularization system, is when entering
When the material particles of system itself are bigger, as shown in Fig. 2, on the basis of Fig. 1, above-mentioned system further includes：Squirrel-cage crushes
Machine 8,
Squirrel-cage crusher 8 is connected by feed hopper 1 with jet microniser 2.
In the present embodiment, material can be carried out just to break by increasing mouse cage crusher, can effectively avoid big material in jet stream
Cycle crushes back and forth between pulverizer and shaping grader, can effectively reduce the particle cycle pulverized time, improve unit
The processing grain amount of jet microniser in time improves unit interval production capacity.That is, by setting squirrel-cage crusher and jet stream
Pulverizer so that material is carried out continuously just broken between jet microniser, between without reciprocal, be it is unidirectional, so as to
Avoid temporal extension.
And to be exactly primary crush be not achieved design object to the principle of the prior art, is crushed with regard to continuous several times, during crushing material
Between it is long.And after being broken at the beginning of having mouse cage crusher, jet microniser, which is dealt with, to be easy for mostly.
Further, as shown in Fig. 2, feed hopper 1 includes：Big hopper 11 and small hopper 12；
Squirrel-cage crusher 8 is connected with big hopper 11, and big hopper 11 is connected with small hopper 12, small hopper 12 and jet mill
Machine 2 is connected.
Above system further includes：First star-shaped feeding machine 13 and the second star-shaped feeding machine 56；
Wherein, big hopper 11 is connected with small hopper 12, including：Big hopper 11 passes through the first star-shaped feeding machine 13 and small hopper
12 are connected；
Shaping feed bin 4 is connected with weighing silo 51, including：Shaping feed bin 4 passes through the second star-shaped feeding machine 56 and material of weighing
Storehouse 51 is connected.
Above system further includes：First conveyer 14 and second conveyor 57,
Wherein, small hopper 12 is connected with jet microniser 2, including：Small hopper 12 passes through the first conveyer 14 and jet stream powder
Broken machine 2 is connected；
Feed inlet of the weighing silo 51 also with shaping grader 52 is connected, including：Weighing silo 51 passes through second conveyor
57 are connected with the feed inlet of shaping grader 52.
In the present embodiment, feed hopper can include big hopper and small hopper, because if only there are one big hopper, such the
As soon as star-shaped feeding machine needs continuously to run, otherwise fracture.The setting of small hopper extends buffer time, just in case the
One star-shaped feeding machine short-duration failure is unlikely to whole system and stops operating.
And if directly big hopper and the first screw conveyor are connected, then big hopper is to the first helical feed arbor
Pressure is too big, and the load of the first screw conveyor is too high, easy overcurrent stop jumping when the first screw conveyor starts, therefore, big
A small hopper can be connected under hopper bottom, so as to avoid big hopper too big to the pressure of the first helical feed arbor, leads to the first spiral shell
It is too high due to loading to revolve conveyer, it is above-mentioned in order to preferably avoid the problem that during startup the problem of easy overcurrent stop jumping, big
The first star-shaped feeding machine is also provided between hopper and small hopper.
Further, as shown in Fig. 2, system further includes：Pulverizer collecting bin 9；
Wherein, whirlwind clarifier 3 is connected with shaping feed bin 4, including：Whirlwind clarifier 3 by pulverizer collecting bin 9 with it is whole
Shape feed bin 4 connects；
Pulverizer collecting bin 9 is also connected with second air-introduced machine 91.
In order to reach without dust pollution, environmentally protective production process, the inside of above-mentioned pulverizer collecting bin, shaping material
The inside in storehouse, the inside in waste product storehouse, finished bin inside at least one dedusting filtering bag is set respectively.
Wherein, the number present invention of dedusting filtering bag set inside each warehouse does not limit, can be according to reality
Increase in demand or reduction.
Further, in order to improve yield, a jet microniser corresponds to more shaping graders 52, can realize graphite
The enlargement of production, at this point, shaping feed bin 4 includes at least one cone, one group of collection material unit 5 of each cone connection.
In specific application, the first above-mentioned conveyer 14 can be：First screw conveyor or the first vibrating feed
Machine；Second conveyor 57 can be：Second screw conveyor or the second oscillating feeder.
The present invention does not limit the specific product of the first conveyer and second conveyor.
When second conveyor 57 is the second screw conveyor, the cylinder of the second screw conveyor by flange directly and shaping
52 pipe connecting flange of grader is connected, and the folder between 52 tubular axis of the tubular axis of the second screw conveyor and shaping grader
Angle is less than or equal to 90 ° and more than or equal to 30 °.
The present invention is due to using two-stage crushing, i.e. squirrel cage crasher and jet microniser, greatly reducing material in jet stream
Residence time in pulverizer, production capacity greatly improve；Secondly it is compared with traditional technology, The present invention reduces crushing and shapings time
Number, rejection number greatly reduces, and high yield rate is up to more than 70%；In addition, the present invention crushes and training time is short, production capacity is being improved
Meanwhile production cost is greatly saved；Finally, due to which the system configured in one piece is reasonable, can be corresponded to a jet microniser more
Platform trimmer can realize the enlargement of graphite production, and negative pressure works in production process is rectified and improved, and without dust pollution is green
Colour circle is protected.
It is introduced below to be crushed using graphite shown in Fig. 2 and the concrete processing procedure of nodularization system：
Material enters aniseed bucket 11 after squirrel-cage crusher 8 is just broken into the particle of below 1mm, then star-like is given through first
Material machine 13 is delivered to small hopper 12, through the quantitative outlet straight tube that material is delivered to jet microniser 2 of the first screw conveyor 14
Duan Shang, under the action of air blower 7, material enters whirlwind clarifier 3, discharging of the qualified material through 3 top of whirlwind clarifier
Pulverizer collecting bin 9 is entered after mouth discharge, returning charge mouth of the underproof material through 3 top of whirlwind clarifier returns to jet stream powder
Broken machine 2 crushes again, recycles successively；Under the action of air-introduced machine 91 by crushing after qualified material transfer to shaping feed bin 4, after
Weighing silo 51 is transported to, then shaping grader 52, object are delivered to through the second screw conveyor 57 through the second star-shaped feeding machine 56
Material completes shaping and the secondary grading of particle in 52 cylinder of shaping grader, underproof under the action of air-introduced machine 6
The waste port at material from the top of shaping grader 52 is discharged to waste product storehouse 54, regular shaped 52 bottom of grader of qualified material
It is discharged into finished bin 53.
Finally it should be noted that：The above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations；To the greatest extent
Pipe is described in detail the present invention with reference to foregoing embodiments, it will be understood by those of ordinary skill in the art that：Its according to
Can so modify to the technical solution recorded in foregoing embodiments either to which part or all technical features into
Row equivalent replacement；And these modifications or replacement, various embodiments of the present invention technology that it does not separate the essence of the corresponding technical solution
The range of scheme.
Claims (8)
1. a kind of graphite crushes and nodularization system, which is characterized in that including：Sequentially connected feed hopper, jet microniser, whirlwind
Grader, shaping feed bin sum aggregate material unit；
The collection material unit includes：Weighing silo, shaping grader, finished bin and waste product storehouse, the shaping feed bin and the title
Heavy burder storehouse is connected, and feed inlet of the weighing silo also with the shaping grader is connected, the plastic section of the shaping grader
Discharge port be connected with the feed inlet of the finished bin, the discharge port of the classification section of the shaping grader and the waste product storehouse
Feed inlet is connected, and the finished bin is connected with the waste product storehouse, the finished bin and the waste product storehouse respectively with a buffering bucket
It is connected；
The waste product storehouse and the shaping feed bin are connected respectively with first air-introduced machine, the jet microniser also with air blower
It is connected；
The system also includes：Squirrel-cage crusher,
The squirrel-cage crusher is connected by the feed hopper with the jet microniser；
The feed hopper includes：Big hopper and small hopper；
The squirrel-cage crusher is connected with the big hopper, and the big hopper is connected with the small hopper, the small hopper with
The jet microniser is connected.
2. graphite according to claim 1 crushes and nodularization system, which is characterized in that the system also includes：First is defeated
Machine and second conveyor are sent,
The small hopper is connected with the jet microniser, including：The small hopper is penetrated by first conveyer with described
Stream pulverizer is connected；
Feed inlet of the weighing silo also with the shaping grader is connected, including：The weighing silo passes through described second
Conveyer is connected with the feed inlet of the shaping grader.
3. graphite according to claim 2 crushes and nodularization system, which is characterized in that the system also includes：First star
Type batcher and the second star-shaped feeding machine；
The big hopper is connected with the small hopper, including：The big hopper by first star-shaped feeding machine with it is described small
Hopper is connected；
The shaping feed bin is connected with the weighing silo, including：The shaping feed bin by second star-shaped feeding machine with
The weighing silo is connected.
4. graphite according to claim 3 crushes and nodularization system, which is characterized in that the system also includes：Pulverizer
Collecting bin；
The whirlwind clarifier is connected with the shaping feed bin, including：The whirlwind clarifier passes through the pulverizer collecting bin
It is connect with the shaping feed bin；
The pulverizer collecting bin is also connected with second air-introduced machine.
5. graphite according to claim 4 crushes and nodularization system, which is characterized in that the pulverizer collecting bin it is interior
Portion, the inside of the shaping feed bin, the inside in the waste product storehouse, the finished bin inside at least one dedusting is set to filter respectively
Bag.
6. graphite according to claim 5 crushes and nodularization system, which is characterized in that the shaping feed bin includes at least one
A cone, each cone connects collects material unit described in one group.
7. graphite according to claim 2 crushes and nodularization system, which is characterized in that
First conveyer is：First screw conveyor or the first oscillating feeder；
The second conveyor is：Second screw conveyor or the second oscillating feeder.
8. graphite according to claim 7 crushes and nodularization system, which is characterized in that if the second conveyor is second
Screw conveyor, the cylinder of second screw conveyor are directly connected by flange with the shaping grader pipe connecting flange,
And the angle between the tubular axis of second screw conveyor and the shaping grader tubular axis be less than or equal to 90 ° and
More than or equal to 30 °.
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| CN201610547694.XA CN106179787B (en) | 2016-07-12 | 2016-07-12 | Graphite crushes and nodularization system |
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|---|---|---|---|
| CN201610547694.XA CN106179787B (en) | 2016-07-12 | 2016-07-12 | Graphite crushes and nodularization system |
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| CN106179787B true CN106179787B (en) | 2018-06-12 |
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| CN110015737A (en) * | 2019-05-05 | 2019-07-16 | 安徽理工大学 | A kind of quantitative automatic add-on system of powdery flocculation medicament and treatment process |
| CN110015738A (en) * | 2019-05-05 | 2019-07-16 | 安徽理工大学 | A kind of mealy medicine quantifies add-on system |
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| CN105013592A (en) * | 2015-08-14 | 2015-11-04 | 吉首大学 | Air suction type grinder for polygonum cuspidatum |
| CN205361601U (en) * | 2016-02-05 | 2016-07-06 | 青岛田庄恒源石墨有限公司 | Can improve vortices air flow balling machine that spherical graphite smashed efficiency |
| CN105621405A (en) * | 2016-02-29 | 2016-06-01 | 成都新柯力化工科技有限公司 | Method for preparing graphene microchip material with high-pressure water jet pulverizer |
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