CN214552962U

CN214552962U - Graphene oxide slurry stirring tank

Info

Publication number: CN214552962U
Application number: CN202120423050.6U
Authority: CN
Inventors: 周步存; 周玉峰; 周仁杰; 高天翔
Original assignee: Huaian Fuxin New Material Co ltd
Current assignee: Huaian Fuxin New Material Co ltd
Priority date: 2021-02-25
Filing date: 2021-02-25
Publication date: 2021-11-02
Anticipated expiration: 2031-02-25

Abstract

The utility model provides a graphite oxide thick liquids agitator tank, which comprises a tank body, the inside of the jar body forms the stirring chamber of graphite alkene thick liquids, stirring driving motor and dispersion driving motor are installed to the top of the jar body, stirring driving motor's power output shaft drive is connected with the (mixing) shaft, be connected with the stirring claw on the (mixing) shaft, dispersion driving motor's power output shaft drive is connected with the dispersion axle, the epaxial dispersion impeller that is connected with of dispersion. The utility model discloses can promote the stirring efficiency to the graphite alkene thick liquids of stirring intracavity, make graphite alkene thick liquids can be dispersed by the intensive mixing, promote the homogeneity of graphite alkene thick liquids, and then do benefit to and promote the off-the-shelf quality of graphite alkene goods.

Description

Graphene oxide slurry stirring tank

Technical Field

The utility model belongs to the technical field of graphite alkene thick liquids stirring, concretely relates to oxidation graphite alkene thick liquids agitator tank.

Background

The graphene slurry stirring process is an important process in the graphene film preparation process, and the uniform stirring and the slurry temperature directly influence the subsequent coating and the quality of the final product. Present agitator tank commonly used only is provided with the agitator shaft device on the one hand usually, and single agitator shaft device can't stir the drier completely and scatter, and the cooling effect of the present agitator tank of on the other hand is not ideal enough, and graphite alkene thick liquids is at stirring in-process temperature very high, and this needs graphite alkene thick liquids to cool off it in the longer time after the stirring finishes, and the manufacturing efficiency of graphite alkene thick liquids has been reduced seriously to the cooling cycle of overlength.

SUMMERY OF THE UTILITY MODEL

Therefore, the to-be-solved technical problem of the utility model is to provide a graphite alkene thick liquids agitator tank can promote the stirring efficiency to the graphite alkene thick liquids of stirring intracavity, makes graphite alkene thick liquids can be dispersed by intensive mixing, promotes the homogeneity of graphite alkene thick liquids, and then does benefit to and promotes the off-the-shelf quality of graphite alkene goods.

In order to solve the problem, the utility model provides a graphite oxide thick liquids agitator tank, which comprises a tank body, the inside of the jar body forms the stirring chamber of graphite alkene thick liquids, stirring driving motor and dispersion driving motor are installed to the top of the jar body, stirring driving motor's power output shaft drive is connected with the (mixing) shaft, be connected with the stirring claw on the (mixing) shaft, dispersion driving motor's power output shaft drive is connected with the dispersion axle, the epaxial dispersion impeller that is connected with of dispersion.

Preferably, the dispersion impeller has a plurality of dispersion impellers, and the plurality of dispersion impellers are arranged at intervals along the height direction of the tank body; and/or a plurality of stirring claws are arranged.

Preferably, the tank is provided with a feeding pipe, and the outlet of the feeding pipe is arranged at the top of the side vertical wall of the tank.

Preferably, the bottom wall and the side vertical wall of the tank body are provided with cooling pipelines, and the top pipeline of the cooling pipelines passes through the intersection position of the feeding pipe and the side vertical wall of the tank body.

Preferably, the cooling pipe spirally surrounds the outer side of the can body along the outer circumferential side of the can body.

Preferably, the cooling pipeline has a cooling water introduction port and a cooling water withdrawal port, wherein a height of the cooling water introduction port is lower than a height of the cooling water withdrawal port.

Preferably, the bottom of the tank body is provided with a discharge port; and/or an observation window is also constructed on the side vertical wall of the tank body; and/or a plurality of support legs are arranged on the outer side wall of the tank body.

Preferably, the dispersion driving motor drives the dispersion shaft to revolve clockwise around a vertical central axis of the tank body; and/or the stirring driving motor drives the stirring shaft to revolve clockwise around the vertical central shaft of the tank body.

Preferably, the dispersion shaft is driven to rotate anticlockwise by the first planetary gear; and/or the stirring shaft is driven to rotate anticlockwise by the second planetary gear.

The utility model provides a pair of graphite alkene thick liquids agitator tank, through the stirring claw and the common setting of dispersion impeller, thereby realized right the graphite alkene thick liquids in the stirring intracavity realize the dispersion when stirring, thereby make the disturbance of graphite alkene thick liquids has the characteristic of combined force, and this can promote the stirring efficiency to the graphite alkene thick liquids of stirring intracavity, makes graphite alkene thick liquids can be dispersed by the intensive mixing, promotes the homogeneity of graphite alkene thick liquids, and then does benefit to and promote the off-the-shelf quality of graphite alkene goods.

Drawings

Fig. 1 is the internal structure schematic diagram of the graphene oxide slurry agitator tank of the embodiment of the utility model.

The reference numerals are represented as:

1. a tank body; 11. a feeding pipe; 12. a support leg; 13. a discharge outlet; 14. an observation window; 15. a stirring chamber; 2. a decentralized drive motor; 21. a dispersion shaft; 22. a dispersion tray; 3. a stirring driving motor; 31. a stirring shaft; 32. a stirring claw; 4. a cooling pipeline; 41. a cooling water introduction port; 42. a cooling water outlet.

Detailed Description

Referring to fig. 1, according to the embodiment of the utility model, a graphene oxide slurry agitator tank is provided, which comprises a tank body 1, the inside of jar body 1 forms the stirring chamber 15 that forms the graphene thick liquids, stirring driving motor 3 and dispersion driving motor 2 are installed to the top of jar body 1, stirring driving motor 3's power output shaft drive is connected with (mixing) shaft 31, be connected with stirring claw 32 on the (mixing) shaft 31, dispersion driving motor 2's power output shaft drive is connected with dispersion axle 21, be connected with dispersion impeller 22 on the dispersion axle 21, it is specific, dispersion axle 21 with the (mixing) shaft 31 is parallel to each other and is located in stirring chamber 15, in order to right the stirring, dispersion are realized to the graphene thick liquids in different regions in the stirring chamber 15. In this technical scheme, through stirring claw 32 and dispersion impeller 22's common setting, thereby realized right realize the dispersion when the graphite alkene thick liquids in stirring chamber 15 stir, thereby make the disturbance of graphite alkene thick liquids has the characteristic of combined force, and this can promote the stirring efficiency to the graphite alkene thick liquids in the stirring chamber, makes graphite alkene thick liquids can be dispersed by the intensive mixing, promotes the homogeneity of graphite alkene thick liquids, and then does benefit to and promotes the off-the-shelf quality of graphite alkene goods.

In some embodiments, the dispersion impeller 22 has a plurality of dispersion impellers 22, and the plurality of dispersion impellers 22 are arranged at intervals along the height direction of the tank body 1, so as to disperse the graphene slurry at different heights, and further improve the uniformity of the slurry at the height; equally reason, stirring claw 32 sets up a plurality ofly, and the setting of a plurality of stirring claws 32 can show promotion stirring efficiency, also can reach the even effect of graphite alkene thick liquids more efficiently.

The tank 1 is provided with a feeding pipe 11, the outlet of which feeding pipe 11 is preferably arranged at the top of the side standing wall of the tank 1 to facilitate the feeding process.

In order to cool the graphene slurry heated by stirring, preferably, the bottom wall and the side vertical wall of the tank body 1 are provided with cooling pipelines 4, and a pipeline at the top of the cooling pipeline 4 passes through the intersection position of the feeding pipe 11 and the side vertical wall of the tank body 1, so that the graphene slurry in the cooling pipeline can be cooled, the cooling period after the stirring in the prior art is finished is effectively shortened, and the overall stirring efficiency is improved. Preferably, the cooling pipeline 4 spirally surrounds the outer side of the tank body 1 along the outer peripheral side of the tank body 1 (specifically, a manner of welding with the tank body 1 can be adopted), and the cooling pipeline 4 spirally surrounds the tank body 1, so that a longer tube pass and continuity of a contact area with the tank body 1 are provided, and heat exchange between cooling water in the cooling pipeline and graphene slurry in the tank body 1 is facilitated.

Further, the cooling pipeline 4 is provided with a cooling water inlet 41 and a cooling water outlet 42, wherein the height of the cooling water inlet 41 is lower than that of the cooling water outlet 42, that is, the cooling water flows through the cooling pipeline 4 from bottom to top, when the bottom of the tank body 1 is provided with the discharge outlet 13, in such a way, the flow direction of the cooling water is in a counter-flow structure, which is more beneficial to improving the cooling efficiency.

An observation window 14 is further formed on the side vertical wall of the tank body 1 so as to observe the slurry stirring dispersion state in real time; the outer side wall of the tank body 1 is provided with a plurality of support legs 12 for reliable and stable connection of the installation carrier.

In order to ensure that the solid material and the liquid material are quickly and uniformly mixed and achieve the effect of primarily breaking particles, the dispersion driving motor 2 drives the dispersion shaft 21 to revolve clockwise around the vertical central axis of the tank body 1, and meanwhile, the dispersion shaft 21 drives the dispersion shaft to rotate anticlockwise through a first planetary gear (not shown in the figure); in order to ensure that the slurry is stirred without dead angles and aggregation and agglomeration phenomena occur, the stirring driving motor 3 drives the stirring shaft 31 to revolve clockwise around the vertical central axis of the tank body 1, and meanwhile, the stirring shaft 31 is driven to rotate anticlockwise through a second planetary gear (not shown in the figure).

It is readily understood by a person skilled in the art that the advantageous ways described above can be freely combined, superimposed without conflict.

The above description is only exemplary of the present invention and should not be construed as limiting the present invention, and any modifications, equivalents and improvements made within the spirit and principles of the present invention are intended to be included within the scope of the present invention. The above is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of modifications and variations can be made without departing from the technical principle of the present invention, and these modifications and variations should also be regarded as the protection scope of the present invention.

Claims

1. The utility model provides a graphite alkene thick liquids agitator tank, its characterized in that, including a jar body (1), the inside of jar body (1) forms stirring chamber (15) for graphite alkene thick liquids, stirring driving motor (3) and dispersion driving motor (2) are installed at the top of jar body (1), the power output shaft drive of stirring driving motor (3) is connected with (mixing) shaft (31), be connected with stirring claw (32) on (mixing) shaft (31), the power output shaft drive of dispersion driving motor (2) is connected with dispersion axle (21), be connected with dispersion impeller (22) on dispersion axle (21).

2. The graphene oxide slurry agitator tank according to claim 1, wherein the dispersion impeller (22) has a plurality of dispersion impellers (22), and the plurality of dispersion impellers (22) are arranged at intervals along a height direction of the tank body (1); and/or a plurality of stirring claws (32) are arranged.

3. The graphene oxide slurry agitator tank of claim 1, wherein the tank body (1) is provided with a feeding pipe (11), and an outlet of the feeding pipe (11) is arranged at the top of the side vertical wall of the tank body (1).

4. The graphene oxide slurry stirring tank according to claim 3, wherein the bottom wall and the side vertical walls of the tank body (1) are provided with cooling pipelines (4), and the top pipelines of the cooling pipelines (4) pass through the intersection positions of the feeding pipes (11) and the side vertical walls of the tank body (1).

5. The graphene oxide slurry agitator tank according to claim 4, wherein the cooling line (4) spirally surrounds the outside of the tank body (1) along the outer circumferential side of the tank body (1).

6. The graphene oxide slurry agitator tank according to claim 4, wherein the cooling pipe (4) has a cooling water introduction port (41) and a cooling water withdrawal port (42), wherein a height of the cooling water introduction port (41) is lower than a height of the cooling water withdrawal port (42).

7. The graphene oxide slurry agitator tank of claim 1, wherein the bottom of the tank body (1) is configured with a discharge opening (13); and/or the side vertical wall of the tank body (1) is also provided with an observation window (14); and/or a plurality of support legs (12) are arranged on the outer side wall of the tank body (1).

8. The graphene oxide slurry agitator tank according to claim 1, wherein the dispersion driving motor (2) drives the dispersion shaft (21) to revolve clockwise around a vertical central axis of the tank body (1); and/or the stirring driving motor (3) drives the stirring shaft (31) to revolve clockwise around the vertical central shaft of the tank body (1).

9. The graphene oxide slurry agitator tank of claim 8, wherein the dispersion shaft (21) is driven to rotate counterclockwise by a first planetary gear; and/or the stirring shaft (31) is driven to rotate anticlockwise by the second planetary gear.