CN205462060U - System is peeled off in mixture of graphite alkene - Google Patents
System is peeled off in mixture of graphite alkene Download PDFInfo
- Publication number
- CN205462060U CN205462060U CN201620191411.8U CN201620191411U CN205462060U CN 205462060 U CN205462060 U CN 205462060U CN 201620191411 U CN201620191411 U CN 201620191411U CN 205462060 U CN205462060 U CN 205462060U
- Authority
- CN
- China
- Prior art keywords
- way valve
- dispersion
- heat exchanger
- homogenizing
- pulverizing
- 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.)
- Withdrawn - After Issue
Links
Abstract
The utility model relates to a system is peeled off in mixture of graphite alkene, this system include disperse system, heat transfer system, heating and cooling system, conveying system, transmission system and control system in advance, still including smashing the homogeneity system, peeling off homogeneity system and ultrasonic wave disperse system, disperse system is including dispersion bucket and stirring dispersion devices in advance, the diaphragm pump that conveying system includes and dispersion bucket is connected, heat transfer system including connect in between diaphragm pump and the dispersion barrel and be connected in the diaphragm pump and first three -way valve and second three -way valve are installed on the connecting tube between diaphragm pump and the dispersion bucket, through the 3rd three - way valve connection between diaphragm pump and first heat exchanger and the second heat exchanger to heat exchanger between the ultrasonic wave disperse system, it including smashing the homogeneity working head, smashes the homogeneity working head and passes through the pipe connection to smash the homogeneity system first three -way valve and second three -way valve, peel off the homogeneity system and peel off the homogeneity working head including installing in what smash homogeneity working head lower extreme.
Description
Technical field
This utility model relates to the production apparatus field of Graphene, particularly to the mixing peel-off device of Graphene.
Background technology
At present, Graphene has the structure of uniqueness and excellent performance, is the material that intensity known to the mankind is the highest.Graphene is the graphite film of monoatomic layer, and its lattice is the bi-dimensional cellular structure being made up of carbon atom.This material has many novel physical characteristics, and it is to be currently known the material that electric conductivity at normal temperatures is best, and electronics movement velocity wherein has reached the 1/300 of the light velocity, considerably beyond general conductor.Additionally, can also be used with Graphene to manufacture composite, battery/super capacitor, hydrogen storage material, field emmision material, hypersensor etc..Cause study interest widely in chemistry, physics and material educational circles in recent years, and achieved with many progress in the preparation of Graphene.
The existing preparation method of Graphene and defect: one, oxidation-reduction method, this method environmental protection, efficient, low cost, extensively application and industrialized production, have a disadvantage in that electronic structure and the perfection of crystal of oxidant meeting heavy damage Graphene, affect electronic property, thus limit its application at accurate microelectronic to a certain extent.Two, the direct stripping method of liquid phase, because of with cheap graphite or expanded graphite as raw material, preparation process is not related to chemical change Graphene and has low cost, simple to operate a, high quality, but to there is also that single-layer graphene productivity is the highest, lamella is reunited serious, need to slough the defects such as stabilizer further.Three, electrochemical stripping method; this method is the earliest with phenyl ring or other aroma system as core; 6 C on phenyl ring or big aromatic rings are made all to be replaced by multistep coupling reaction; move in circles; make aroma system become big, obtain the Graphene of the planar structure of certain size, scale can be met and prepare the requirement of high-quality, large-area graphene; but present stage is because of its higher cost, complicated technique and is accurately controlled processing conditions and constrains this method and prepare the development of Graphene, needs to be studied further.Four, biomass catalyzing, first C atom is allowed to penetrate in ruthenium under 1150 ° of C, it is subsequently cooled to 850 ° of C, the a large amount of carbon atoms before absorbed will float to ruthenium surface, form the monolayer carbon atom " isolated island " of lens shape in whole stromal surface, " isolated island " gradually grows up, and finally grows up to one layer of complete Graphene, but it is the most in uneven thickness to adopt the graphene platelet produced in this way, and the bonding between Graphene and substrate can affect the characteristic of prepared graphene platelet.
In sum, the various preparation methoies of Graphene all contain bigger limitation, as many in fault of construction, electric conductivity is poor, production capacity is low, be difficult to large-scale production, cost high, quality is low.
Utility model content
The applicant is for the disadvantages mentioned above of prior art, study and design, a kind of Graphene mixing stripping system is provided, it uses macroscopic view dispersion mixing/microcosmic to pulverize homogenizing and microcosmic peels off homogenizing three phases, realize to fully the pulverizing of Graphene, disperse, peel off, homogenizing, significantly improve production efficiency and the quality of Graphene.
In order to solve the problems referred to above, this utility model following scheme of employing:
A kind of Graphene mixing stripping system, including pre-dispersed system, heat-exchange system, heating and cooling system, induction system, drive system and control system, also includes pulverizing homogeneous system, peeling off homogeneous system and ultrasound wave disperse system；Described pre-dispersed system includes disperseing bucket and dispersed with stirring device, described induction system includes the membrane pump being connected with dispersion bucket, described heat-exchange system includes the First Heat Exchanger being connected between membrane pump and dispersion bucket and is connected to the second heat exchanger between membrane pump and described ultrasound wave disperse system, on connection pipeline between described membrane pump and dispersion bucket, the first three-way valve and the second three-way valve are installed, are connected by the 3rd three-way valve between membrane pump with First Heat Exchanger and the second heat exchanger；Described pulverizing homogeneous system includes the pulverizing homogenizing work head being connected with drive system, the side pulverizing homogenizing work head connects described first three-way valve and the second three-way valve by pipeline, described stripping homogeneous system includes being installed on the stripping homogenizing work head pulverizing homogenizing work head lower end, and described ultrasound wave disperse system includes the ultrasound wave dispersion pipe being connected to the second heat exchanger and peeling off between homogenizing work head.
Further improvement as technique scheme:
Described dispersed with stirring device includes the puddler driven by air motor and is installed on the dispersion impeller of puddler end, and described puddler tilts to be placed in described dispersion bucket.
Described dispersion impeller includes disk body and is installed on the stirring sheet of disk body side face, adjacent stirring sheet relative to disk body towards on the contrary.
Described pulverizing homogenizing work head include the screen cloth, stator and the rotor that are installed in homogenizing bucket, rotor include center drive shaft and centered by drive shaft outside spaced apart cutting ring, the perisporium of drive shaft is provided with cutting blade；Described stator includes the split ring that internal and external partition is arranged, the cutting ring of rotor is alternate to be placed in adjacent split ring.
On inside and outside cutting ring, its circle spacing is provided with slot segmentation, described slot segmentation relative to the radial direction of cutting ring with drift angle α；On inside and outside split ring, its circle spacing is provided with the second slot segmentation, the second slot segmentation being radially arranged along split ring.
Described stripping homogenizing work head includes the revolving cup being installed in the pump housing, and revolving cup includes the rotating shaft at center and is connected to, by gripper shoe, the rotating cylinder that rotating shaft is peripheral, and the sidewall of described rotating cylinder is evenly equipped with through hole.
The Graphene mixing stripping means of a kind of Graphene mixing stripping system utilized described in claim, comprises the following steps:
The first step, Graphene solvent is added in dispersion bucket, start the driving motor of pre-dispersed system, membrane pump, open the first three-way valve, the second three-way valve and three-way valve, make membrane pump, dispersion bucket and First Heat Exchanger connection, form the Guan Bi macroscopic view dispersion mixing blood circulation of dispersion bucket-membrane pump-First Heat Exchanger-dispersion bucket, heating and cooling system First Heat Exchanger is heated；
Second step, start the driving motor pulverizing homogenizing work head, regulate the first three-way valve, the second three-way valve and three-way valve, make membrane pump with pulverize homogenizing work head and First Heat Exchanger connect, pulverizes homogenizing work head with disperse bucket connect, the Guan Bi microcosmic forming dispersion bucket-pulverizing homogenizing work head-membrane pump-First Heat Exchanger-dispersion bucket pulverizes homogenisation cycle system, heats and First Heat Exchanger is cooled down by cooling system；
3rd step, regulate the first three-way valve, second three-way valve and three-way valve, membrane pump is made to connect with pulverizing homogenizing work head and the second heat exchanger, dispersion bucket connects with pulverizing homogenizing work head, the microcosmic forming dispersion bucket-pulverizing homogenizing work head-membrane pump the-the second heat exchanger-ultrasound wave dispersion pipe-stripping homogenizing work head peels off homogeneous system, second heat exchanger is cooled down by heating and cooling system, Graphene after cooling enters ultrasound wave dispersion pipe and carries out ultrasound wave dispersion, Graphene after ultrasound wave dispersion pipe disperses enters peels off homogenizing work head, complete the Graphene after peeling off homogenizing from the outlet tube output being connected with stripping homogenizing work head；
4th step, after the working in dispersion of Graphene completes, injects cleanout fluid in dispersion bucket, regulation regulation the first three-way valve, the second three-way valve and three-way valve, starting air motor and drive system, clear up the residue in pipeline, the sewage after cleaning is discharged from outlet tube.
Further improvement as technique scheme:
In the described first step, the working time scope of Guan Bi macroscopic view dispersion mixing blood circulation is: 25-35 minute；The working time scope closing microcosmic pulverizing homogenisation cycle system in described second step is: 15-25 minute；In described 3rd step, the working time scope of microcosmic stripping homogeneous system is: 15-25 minute.
In the described first step, the working time of Guan Bi macroscopic view dispersion mixing blood circulation is 30 minutes；The working time closing microcosmic pulverizing homogenisation cycle system in described second step is 20 minutes；In described 3rd step, the working time of microcosmic stripping homogeneous system is: 20 minutes.
Of the present utility model have the technical effect that
When this utility model uses, the mixing to Graphene is divided into three phases.
This utility model pulverizes the homogenizing stage by macroscopic view dispersion mixing stage, microcosmic and microcosmic peels off the homogenizing stage, after macroscopic view dispersed with stirring, under the effect of the strong mechanical shear stress in superfine grinding workpiece, the aggregates such as the Graphene powder ball in solution are pulverized further and broken up, obtain the most tiny powder granule, and be uniformly distributed in solution, thus reach the effect of refinement and homogenizing, it is remarkably improved slurry batch mixing efficiency；In superfine grinding workpiece, plug knife run up formed film like structures, under the hydraulic shearing forces effect of high intensity, it is possible to the Graphene micropowder in solution and aggregate are broken up further and peeled off, fully Graphene is carried out lamellar stripping, and be uniformly distributed in solution.
Using this utility model to carry out Graphene mixing dispersion, its advantage has:
1, dispersive process all completes in closed environment, produces without dust, improves working environment；
2, ultra high shear dispersion principle, it is achieved microcosmic dispersed ultrafine；
3, compare traditional handicraft, can shorten working hours, improve production efficiency；
4, by pulverizing, disperse, peel off, homogenizing is organically combined, multiple discrete form combines, and learns from other's strong points to offset one's weaknesses, and improves scattered effect；
5, multicycle pipe design, can select to pulverize number of times and the number of times of whole flow process of homogenizing according to disperseing the effect that；
6, pipeline is distributed two heat exchanger tubes, as required the serosity in dispersion can be cooled down or heats；
7, join hot and cold water switch, carry Cooling Water at any time and add hot water；
8, the arrangement design comparison of pipeline is reasonable, can meet total enclosing and produce, have and can meet on-line cleaning requirement.
Accompanying drawing explanation
Fig. 1 is front view of the present utility model.
Fig. 2 is utility model works principle schematic.
Fig. 3 is three-dimensional structure diagram of the present utility model.
Fig. 4 is the three-dimensional structure diagram of dispersed with stirring device in this utility model.
Fig. 5 is the three-dimensional structure diagram of dispersion impeller in this utility model.
Fig. 6 is the three-dimensional structure diagram of the rotor pulverizing homogenizing work head in this utility model.
Fig. 7 is the rotor main view pulverizing homogenizing work head in this utility model.
Fig. 8 is the three-dimensional structure diagram of the stator pulverizing homogenizing work head in this utility model.
Fig. 9 is the three-dimensional structure diagram pulverizing homogenizing work head in this utility model.
Figure 10 is the three-dimensional structure diagram pulverizing homogenizing work head in this utility model.
Figure 11 is the three-dimensional structure diagram peeling off homogenizing work head in this utility model.
Figure 12 is another three-dimensional structure diagram peeling off homogenizing work head.
Figure 13 is the three-dimensional structure diagram of ultrasound wave dispersion pipe in this utility model.
In figure: 1, pre-dispersed system；2, First Heat Exchanger；3, the first three-way valve；4, the second three-way valve；5, the 3rd three-way valve；6, homogenizing work head is pulverized；600, homogenizing bucket；601, screen cloth；602, stator；6021, split ring；6022, the second slot segmentation；603, rotor；6031, drive shaft；6032, cutting ring；6033, cutting blade；6034, the first slot segmentation；7, homogenizing work head is peeled off；701, the pump housing；702, revolving cup；7021, rotating shaft；7022, gripper shoe；7023, rotating cylinder；7024, through hole；8, membrane pump；9, the second heat exchanger；10, sound wave dispersion pipe；100, dispersion bucket；101, dispersed with stirring device；1011, air motor；1012, puddler；1013, dispersion impeller；10131, disk body；10132, stirring sheet；11, heating and cooling system；12, drive system；13, Guan Bi macroscopic view dispersion mixing blood circulation；14, Guan Bi microcosmic pulverizes homogenisation cycle system；15, microcosmic peels off homogeneous system；16, outlet tube.
Detailed description of the invention
Below in conjunction with the accompanying drawings detailed description of the invention of the present utility model is described further.
As shown in Figure 1, Figure 2 and Figure 3, the Graphene mixing stripping system of the present embodiment, including pre-dispersed system 1, heat-exchange system, heating and cooling system 11, induction system, drive system 12 and control system, also include pulverizing homogeneous system, peeling off homogeneous system and ultrasound wave disperse system；Pre-dispersed system 1 includes disperseing bucket 100 and dispersed with stirring device 101, induction system includes the membrane pump 8 being connected with dispersion bucket 100, heat-exchange system includes the First Heat Exchanger 2 being connected between membrane pump 8 and dispersion bucket 100 and the second heat exchanger 9 being connected between membrane pump 8 and ultrasound wave disperse system, on connection pipeline between membrane pump 8 and dispersion bucket 100, the first three-way valve 3 and the second three-way valve 4 is installed, is connected by the 3rd three-way valve 5 between membrane pump 8 with First Heat Exchanger 2 and the second heat exchanger 9；Pulverize the pulverizing homogenizing work 6 that homogeneous system includes being connected with drive system 12, the side pulverizing homogenizing work 6 connects the first three-way valve 3 and the second three-way valve 4 by pipeline, peeling off homogeneous system to include being installed on the stripping homogenizing work 7 pulverizing homogenizing work 6 lower end, ultrasound wave disperse system includes the ultrasound wave dispersion pipe 10 being connected to the second heat exchanger 9 and peeling off between homogenizing work 7.
As shown in Figure 4, Figure 5, in pre-dispersed system 1, dispersed with stirring device 101 includes the puddler 1012 driven by air motor 1011 and is installed on the dispersion impeller 1013 of puddler 1012 end, and puddler 1012 tilts to be placed in dispersion bucket 100.For improving dispersion effect, dispersion impeller 1013 includes disk body 10131 and is installed on the stirring sheet 10132 of disk body 10131 side face, the adjacent stirring relative disk body 10131 of sheet 10132 towards on the contrary.
As shown in Figure 2 and Figure 3, the Graphene mixing stripping means of the present embodiment, comprise the following steps:
The first step, Graphene solvent is added in dispersion bucket 100, start the driving motor of pre-dispersed system 1, membrane pump 8, open first three-way valve the 3, second three-way valve 4 and three-way valve 5, membrane pump 8, dispersion bucket 100 and First Heat Exchanger 2 is made to connect, forming the Guan Bi macroscopic view dispersion mixing blood circulation 13 of dispersion bucket 100-membrane pump 8-First Heat Exchanger 2-dispersion bucket 100, First Heat Exchanger 2 is heated by heating and cooling system 11；Gradually being joined in agitator tank by graphene powder, driven by motor dispersion impeller carries out preliminary dispersion to graphene powder, and First Heat Exchanger 2 is heated by heating and cooling system, improves graphene powder dissolubility in a solvent, it is possible to fully dissolve.
Second step, start the driving motor pulverizing homogenizing work 6, regulate the first three-way valve 3, second three-way valve 4 and three-way valve 5, membrane pump 8 is made to connect with pulverizing homogenizing work 6 and First Heat Exchanger 2, pulverize homogenizing work 6 to connect with dispersion bucket 100, the Guan Bi microcosmic forming dispersion bucket 100-pulverizing homogenizing work head 6-membrane pump 8-First Heat Exchanger 2-dispersion bucket 100 pulverizes homogenisation cycle system 14, First Heat Exchanger 2 is cooled down by heating and cooling system 11, reduce the temperature of solution, the loop making Guan Bi can work repeatedly, thus improve the effect pulverizing homogenizing of Graphene；
3rd step, regulate the first three-way valve 3, second three-way valve 4 and three-way valve 5, membrane pump 8 is made to connect with pulverizing homogenizing work 6 and the second heat exchanger 9, dispersion bucket 100 connects with pulverizing homogenizing work 6, the microcosmic forming dispersion bucket 100-pulverizing homogenizing work head 6-membrane pump 8-the second heat exchanger 9-ultrasound wave dispersion pipe 10-stripping homogenizing work 7 peels off homogeneous system 15, second heat exchanger 9 is cooled down by heating and cooling system 11, Graphene after cooling enters ultrasound wave dispersion pipe 10 and carries out ultrasound wave dispersion, Graphene after ultrasound wave dispersion pipe 10 disperses enters peels off homogenizing work 7, complete the Graphene after peeling off homogenizing to export from stripping homogenizing work 7 outlet tube 16 being connected；
After whole mixing dispersion flow process completes, if needing to improve dispersion effect, can be circulated and spreading the work.
4th step, after the working in dispersion of Graphene completes, injects cleanout fluid in dispersion bucket 100, regulation regulation first three-way valve the 3, second three-way valve 4 and three-way valve 5, starting air motor 1011 and drive system 3, clear up the residue in pipeline, the sewage after cleaning is discharged from outlet tube 16.
In this utility model, in the first step, the working time scope of Guan Bi macroscopic view dispersion mixing blood circulation 13 is: 25-35 minute；The working time scope closing microcosmic pulverizing homogenisation cycle system 14 in second step is: 15-25 minute；In 3rd step, the working time scope of microcosmic stripping homogeneous system 15 is: 15-25 minute.
In this utility model, the best effort time of Guan Bi macroscopic view dispersion mixing blood circulation 13 is 30 minutes, and the best effort time of Guan Bi microcosmic pulverizing homogenisation cycle system 14 is 20 minutes, and the best effort time of microcosmic stripping homogeneous system 15 is 20 minutes.
As shown in Fig. 6 to Figure 10, in this utility model, pulverize screen cloth 601, stator 602 and rotor 603 that homogenizing work 6 includes being installed in homogenizing bucket 600, rotor 603 include center drive shaft 6031 and centered by drive shaft 6031 outside spaced apart cutting ring 6032, the perisporium of drive shaft 6031 is provided with cutting blade 6033；Stator 602 includes the split ring 6021 that internal and external partition is arranged, the cutting ring 6032 of rotor 603 is alternate to be placed in adjacent split ring 6021.On inside and outside cutting ring 6032, its circle spacing being provided with the first slot segmentation 6034, the radial direction of the first relative cutting ring 6032 of slot segmentation 6034 is with drift angle α；On inside and outside split ring 6021, its circle spacing is provided with the second slot segmentation 6022, the second slot segmentation 6022 being radially arranged along split ring 6021.
When pulverizing homogenizing work 6 work, start dispersion motor, when the Graphene mixed liquor of premixing enters in this working chamber, motor-driven is to axle system, make tooth-like rotor 603 high speed rotating, smaller due to rotor 603 and the line space design of screen cloth 601, processing is all to leave certain edge of a knife, and shape has a certain degree, pre-dispersed graphene solution further can be pulverized homogenizing work, and adjusted by the switch of ball valve in pipeline, graphene solution can be circulated pulverizing homogenizing repeatedly, now logical cooling water in heat exchanger, can effectively reduce the temperature of solution in crushing process, increase the number of times pulverizing homogenizing further, the effect making pulverizing homogenizing is more preferable.
As shown in Figure 11, Figure 12, peeling off the revolving cup 702 that homogenizing work 7 includes being installed in the pump housing 701, revolving cup 702 is included the rotating shaft 7021 at center and is connected to the rotating cylinder 7023 of rotating shaft 7021 periphery by gripper shoe 7022, and the sidewall of rotating cylinder 7023 is evenly equipped with through hole 7024.
Peeling off homogenizing work head when using, graphene solution enters from lower port, by the high speed rotating of revolving cup 702 solution in the pump housing 701 carries out peeling off homogenizing, then discharges through the pipe outlet of side.
The operation principle of ultrasound wave disperse system of the present utility model is: when ultrasound wave is propagated in the solution, by mechanism, cavitation and heat effect, produces the series of effects such as mechanics, calorifics, optics, electricity and chemistry.The most high-power ultrasound wave, can produce strong cavitation, thus be partially formed TRANSIENT HIGH TEMPERATURE, high pressure, vacuum and microjet.Ultra sonic machinery effect can make material make violent forced movement, produces unidirectional force and accelerates the transmission of material, diffusion, can replace mechanical agitation, material can be made from sur-face peeling, it is achieved ultrasound wave disperses.The generation of ultrasonic disperse effect to be then associated with cavitation mechanism, and acoustic cavitation refers under acoustic wave action, a series of dynamic processes that the micro-bubble (hole) being present in liquid is occurred: vibrate, expand, shrink or even collapse.Occurring at cavitation, the state of liquid local changes a lot, and can produce extreme high temperature and high pressure.When supersonic generator output high voltage is added on Under Ultrasonic Vibration mover, after ticker horn mechanical activation amplitude amplifies under dispensing implement effect, carry out strong dispersion in the duct and process.
This utility model arranges two groups of pipeline heat-exchange systems: reasonably places two groups of heat exchangers in the arrangement of pipeline, heats the graphene solution in work process or cool down.
Heating in this utility model and refrigeration system 11: configure a hot and cold water exchanger, coordinate heat exchanger work in pipeline, controls the temperature of graphene solution in work process.
This utility model also includes intelligence control system: whole workflow is all to be controlled by electric cabinet, according to the demand of client, selects the button on control panel, controls the workflow needed.
Embodiment provided above is better embodiment of the present utility model, only it is used for convenient explanation this utility model, not this utility model is made any pro forma restriction, any art has usually intellectual, if in the range of without departing from the carried technical characteristic of this utility model, utilize the Equivalent embodiments that the done local of this utility model disclosed technology content is changed or modified, and without departing from technical characteristic content of the present utility model, all still fall within the range of this utility model technical characteristic.
Claims (6)
1. a Graphene mixing stripping system, including pre-dispersed system (1), heat-exchange system, heating and cooling system (11), induction system, drive system (12) and control system, it is characterised in that: also include pulverizing homogeneous system, peeling off homogeneous system and ultrasound wave disperse system；Described pre-dispersed system (1) includes disperseing bucket (100) and dispersed with stirring device (101), described induction system includes the membrane pump (8) being connected with dispersion bucket (100), described heat-exchange system includes the First Heat Exchanger (2) being connected between membrane pump (8) and dispersion bucket (100) and the second heat exchanger (9) being connected between membrane pump (8) and described ultrasound wave disperse system, on connection pipeline between described membrane pump (8) and dispersion bucket (100), the first three-way valve (3) and the second three-way valve (4) are installed, it is connected by the 3rd three-way valve (5) between membrane pump (8) with First Heat Exchanger (2) and the second heat exchanger (9)；Described pulverizing homogeneous system includes pulverizing homogenizing work head (6) being connected with drive system (12), the side pulverizing homogenizing work head (6) connects described first three-way valve (3) and the second three-way valve (4) by pipeline, described stripping homogeneous system includes being installed on stripping homogenizing work head (7) pulverizing homogenizing work head (6) lower end, and described ultrasound wave disperse system includes the ultrasound wave dispersion pipe (10) being connected to the second heat exchanger (9) and peeling off between homogenizing work head (7).
2. according to the Graphene mixing stripping system described in claim 1, it is characterized in that: described dispersed with stirring device (101) includes the puddler (1012) driven by air motor (1011) and the dispersion impeller (1013) being installed on puddler (1012) end, described puddler (1012) tilts to be placed in described dispersion bucket (100).
3. according to the Graphene mixing stripping system described in claim 2, it is characterized in that: described dispersion impeller (1013) includes disk body (10131) and is installed on the stirring sheet (10132) of disk body (10131) side face, adjacent stirring sheet (10132) relatively disk body (10131) towards on the contrary.
4. according to the Graphene mixing stripping system described in claim 1, it is characterized in that: described pulverizing homogenizing work head (6) includes screen cloth (601), stator (602) and the rotor (603) being installed in homogenizing bucket (600), rotor (603) include center drive shaft (6031) and centered by drive shaft (6031) outside spaced apart cutting ring (6032), the perisporium of drive shaft (6031) is provided with cutting blade (6033)；Described stator (602) includes the split ring (6021) that internal and external partition is arranged, the cutting ring (6032) of rotor (603) is alternate to be placed in adjacent split ring (6021).
5. according to the Graphene mixing stripping system described in claim 4, it is characterized in that: on inside and outside cutting ring (6032), its circle spacing is provided with the first slot segmentation (6034), the radial direction of described first slot segmentation (6034) cutting ring (6032) relatively is with drift angle (α)；On inside and outside split ring (6021), its circle spacing is provided with the second slot segmentation (6022), the second slot segmentation (6022) being radially arranged along split ring (6021).
6. according to the Graphene mixing stripping system described in claim 1, it is characterized in that: described stripping homogenizing work head (7) includes the revolving cup (702) being installed in the pump housing (701), revolving cup (702) includes the rotating shaft (7021) at center and is connected to, by gripper shoe (7022), the rotating cylinder (7023) that rotating shaft (7021) is peripheral, and the sidewall of described rotating cylinder (7023) is evenly equipped with through hole (7024).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620191411.8U CN205462060U (en) | 2016-03-11 | 2016-03-11 | System is peeled off in mixture of graphite alkene |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620191411.8U CN205462060U (en) | 2016-03-11 | 2016-03-11 | System is peeled off in mixture of graphite alkene |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205462060U true CN205462060U (en) | 2016-08-17 |
Family
ID=56657500
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620191411.8U Withdrawn - After Issue CN205462060U (en) | 2016-03-11 | 2016-03-11 | System is peeled off in mixture of graphite alkene |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205462060U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105727811A (en) * | 2016-03-11 | 2016-07-06 | 无锡职业技术学院 | Hybrid graphene stripping system and hybrid graphene stripping method |
| CN106430168A (en) * | 2016-08-31 | 2017-02-22 | 无锡东恒新能源科技有限公司 | Preparation system of graphene slurry |
| CN107522192A (en) * | 2017-07-11 | 2017-12-29 | 南通大学 | Continuous stream vertical surface type liquid phase cutting method |
| CN110193329A (en) * | 2019-05-17 | 2019-09-03 | 葛志强 | A kind of hypergravity coupling prepares the device of two-dimension nano materials |
| CN110467178A (en) * | 2019-09-29 | 2019-11-19 | 威海云山科技有限公司 | A method of preparing graphene |
| RU196276U1 (en) * | 2019-10-08 | 2020-02-21 | Федеральное государственное унитарное предприятие "Центральный научно-исследовательский институт конструкционных материалов "Прометей" имени И.В. Горынина Национального исследовательского центра "Курчатовский институт" (НИЦ "Курчатовский институт" - ЦНИИ КМ "Прометей") | DEVICE FOR ULTRASONIC DISPERSION OF METAL POWDERS |
| CN114345510A (en) * | 2021-12-23 | 2022-04-15 | 上海天新纳米技术有限公司 | Oil blanket nanometer PVA breaker for fibre production based on cavitation effect |
-
2016
- 2016-03-11 CN CN201620191411.8U patent/CN205462060U/en not_active Withdrawn - After Issue
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105727811A (en) * | 2016-03-11 | 2016-07-06 | 无锡职业技术学院 | Hybrid graphene stripping system and hybrid graphene stripping method |
| CN106430168A (en) * | 2016-08-31 | 2017-02-22 | 无锡东恒新能源科技有限公司 | Preparation system of graphene slurry |
| CN107522192A (en) * | 2017-07-11 | 2017-12-29 | 南通大学 | Continuous stream vertical surface type liquid phase cutting method |
| CN107522192B (en) * | 2017-07-11 | 2019-08-16 | 南通大学 | Continuous flow vertical surface type liquid phase cutting method |
| CN110193329A (en) * | 2019-05-17 | 2019-09-03 | 葛志强 | A kind of hypergravity coupling prepares the device of two-dimension nano materials |
| CN110467178A (en) * | 2019-09-29 | 2019-11-19 | 威海云山科技有限公司 | A method of preparing graphene |
| CN110467178B (en) * | 2019-09-29 | 2022-07-22 | 威海云山科技有限公司 | Method for preparing graphene |
| RU196276U1 (en) * | 2019-10-08 | 2020-02-21 | Федеральное государственное унитарное предприятие "Центральный научно-исследовательский институт конструкционных материалов "Прометей" имени И.В. Горынина Национального исследовательского центра "Курчатовский институт" (НИЦ "Курчатовский институт" - ЦНИИ КМ "Прометей") | DEVICE FOR ULTRASONIC DISPERSION OF METAL POWDERS |
| CN114345510A (en) * | 2021-12-23 | 2022-04-15 | 上海天新纳米技术有限公司 | Oil blanket nanometer PVA breaker for fibre production based on cavitation effect |
| CN114345510B (en) * | 2021-12-23 | 2022-12-13 | 上海天新纳米技术有限公司 | Oil blanket nanometer PVA breaker for fibre production based on cavitation effect |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205462060U (en) | System is peeled off in mixture of graphite alkene | |
| CN105727811A (en) | Hybrid graphene stripping system and hybrid graphene stripping method | |
| CN102294192A (en) | Ultrasonic mixing device | |
| CN108295795B (en) | Conduction oil heating low-loss stirring reaction kettle | |
| CN104477882A (en) | A vortex graphene stripping device, a graphene producing system and a producing method | |
| CN106564885A (en) | Jet device for continuous preparation of graphene and method thereof | |
| CN202246459U (en) | Water-soluble fertilizer production equipment | |
| CN107265444B (en) | A kind of complexes and method that graphene is prepared using jet | |
| CN206913417U (en) | A kind of concrete central mix plant of municipal works | |
| CN106422902A (en) | Efficient stirring device | |
| CN201832590U (en) | System for homogenizing slurry material of battery with high efficiency | |
| CN212348745U (en) | Water-based resin synthesizer capable of fully stirring | |
| CN104437310B (en) | A kind of reactor with cooling device | |
| CN106179094A (en) | The dispersed system of a kind of slurry automatization | |
| CN207551918U (en) | Graphene production equipment | |
| CN209210398U (en) | Stripping system for graphene production | |
| CN208277238U (en) | The mixing of PE cable cover(ing) masterbatch production squeezes out integrated apparatus | |
| CN205235968U (en) | Improved generation reaction still | |
| CN112808077A (en) | Permeable concrete reinforcing agent production equipment and method thereof | |
| CN206535635U (en) | A kind of graphene slurry production line with real-time traffic monitoring function | |
| CN206253090U (en) | A kind of high solids content Graphene slurry automates premixing system | |
| CN206304640U (en) | A kind of agitating device for being easy to clean | |
| CN206082401U (en) | Graphite alkene thick liquids integration disperse system | |
| CN204564128U (en) | Two hybrid industrial reaction still | |
| CN205182734U (en) | High -efficient reation kettle with refrigerating plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160817 Effective date of abandoning: 20180112 |
|
| AV01 | Patent right actively abandoned |