CN215586272U - Agitating unit is used in production of graphite liquid - Google Patents
Agitating unit is used in production of graphite liquid Download PDFInfo
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- CN215586272U CN215586272U CN202121225616.0U CN202121225616U CN215586272U CN 215586272 U CN215586272 U CN 215586272U CN 202121225616 U CN202121225616 U CN 202121225616U CN 215586272 U CN215586272 U CN 215586272U
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Abstract
The utility model belongs to the field of graphite liquid production lines, and particularly relates to a stirring device for graphite liquid production, which comprises a base and a dust collecting pipe, wherein the top end of the base is sequentially provided with a support frame, a pull cylinder, a filling box and a pulse dust collector, the top end of the support frame is sequentially provided with a dry powder stirring tank, a mounting frame and an auxiliary material stirring tank, the top end of the mounting frame is provided with a vibrating screen, the dust collecting pipe is positioned above the vibrating screen, the top of the dry powder stirring tank is provided with a first dispersing machine, the top of the auxiliary material stirring tank is provided with a second dispersing machine, and the bottom end of the dry powder stirring tank is provided with a first discharge pipe. Is worthy of popularization and application.
Description
Technical Field
The utility model relates to the technical field of graphite liquid production lines, in particular to a stirring device for graphite liquid production.
Background
The lubricated liquid production technology of graphite for the piercing press mainly grinds the process at the stirring, prevents that the later stage from producing the precipitation phenomenon, and current technology is mostly impeller rotation in the agitator tank and makes various batching fuse in aqueous, and stirring rotational speed because of the impeller formula is low, graphite liquid viscosity is big, and the poor easy sediment of batching emulsification effect can only be solved through extension churning time, so cause the production efficiency end again. The traditional process for producing the agglomerate easily when the graphite meets water adopts a nanoscale conical grinding machine for secondary grinding, the graphite is seriously precipitated before emulsification, and the grinding head of the grinding machine is often blocked, so that manual cleaning is needed, and time and labor are wasted; liquid is circulated in production links and is pushed to carry out by adopting a conventional gear pump, and the gear pump is frequently replaced, damaged and replaced due to high graphite viscosity and rapid hardening after precipitation, so that the stirring device for producing the graphite liquid is provided.
SUMMERY OF THE UTILITY MODEL
The utility model provides a stirring device for graphite liquid production, which aims to solve the problems in the background technology.
In order to achieve the purpose, the utility model adopts the following technical scheme:
a stirring device for graphite liquid production comprises a base and a dust collecting pipe, wherein a support frame, a drawing cylinder, a filling box and a pulse dust collector are sequentially arranged at the top end of the base, a dry powder stirring tank, a mounting frame and an auxiliary material stirring tank are sequentially arranged at the top end of the support frame, a vibrating screen is installed at the top end of the mounting frame, the dust collecting pipe is positioned above the vibrating screen, a first dispersing machine is installed at the top of the dry powder stirring tank, a second dispersing machine is installed at the top of the auxiliary material stirring tank, a first discharging pipe is arranged at the bottom end of the dry powder stirring tank, a first conveying pipe is connected to the bottom end of the first discharging pipe through a first automatic valve, a first pneumatic diaphragm pump is connected to one end, away from the first automatic valve, of the first conveying pipe, a discharging end of the first pneumatic diaphragm pump is connected with the vibrating screen through a second conveying pipe, and a third conveying pipe is connected to the discharging end of the vibrating screen, the third conveying pipeline extends to the inside of auxiliary material agitator tank, the bottom of auxiliary material agitator tank is provided with the second discharging pipe, and the bottom of second discharging pipe is connected with the fourth conveying pipeline through second automatic valve, and the one end that second automatic valve was kept away from to the fourth conveying pipeline is connected with the pneumatic diaphragm pump of second, the discharge end of the pneumatic diaphragm pump of second is connected with the fifth conveying pipeline, and the fifth conveying pipeline extends to the inside of drawing the jar, draw the top of jar and install the emulsion machine, the bottom of drawing the jar is provided with the third discharging pipe, and the side of third discharging pipe is connected with the sixth conveying pipeline through the third automatic valve, and the one end that third automatic valve was kept away from to the sixth conveying pipeline is connected with the pneumatic diaphragm pump of third, the discharge end of the pneumatic diaphragm pump of third is connected with the seventh conveying pipeline, and the seventh conveying pipeline extends to the inside of irritating the case.
Preferably, the top of the dry powder stirring tank is provided with a first dust hood, the top of the auxiliary material stirring tank is provided with a second dust hood, the dust collecting pipe is connected with the first dust hood through a first connecting pipe, the dust collecting pipe is connected with the second dust hood through a second connecting pipe, and the dust collecting pipe is connected with the pulse dust collector through a third connecting pipe.
Preferably, an electric hoist is mounted right above the pulling cylinder.
The utility model has the beneficial effects that:
through the matching action of a base, a support frame, a dry powder stirring tank, a first dispersing machine, a mounting frame, a vibrating screen, an auxiliary material stirring tank, a second dispersing machine, a dust collecting pipe, a pulling cylinder, an emulsifying machine, an electric hoist, a filling box, a pulse dust collector, a first pneumatic diaphragm pump, a second pneumatic diaphragm pump and a third pneumatic diaphragm pump, the traditional impeller is replaced by a high-speed dispersing machine, and the graphite powder is crushed and quickly stirred; the pipeline material circulation adopts a pneumatic diaphragm pump to reduce equipment damage caused by graphite contact; a high-speed emulsifying machine is added at a discharge port, filling is carried out after full emulsification and batching, the automation degree is high, and the manual labor intensity is low;
the high-speed dispersion machine is similar to the principle of a wall breaking machine, the blade cutter rotates to generate backflow in the tank, graphite with large particles is broken by the blade and can be fully fused with water, a vibrating screen is added to screen out graphite blocks and sundries which cannot be broken, and a grinding machine is directly omitted;
the high rotating speed can reduce the stirring time and improve the efficiency;
the direct contact of graphite is reduced by feeding with a pneumatic diaphragm pump, and the safety factor is increased on the site of water operation by changing electric into pneumatic; a high-speed emulsifying machine is added before the ingredients are fully stirred and filled, the process is suitable for the emulsifying operation of the liquid with high viscosity, and the graphite liquid can be ensured not to precipitate for a long time after the emulsification, so that the use quality requirement of the perforating machine is not influenced;
the length of a pipeline from feeding and stirring to an emulsifying machine is shortened through process optimization and short flow design, and the agglomeration phenomenon before graphite emulsification is further reduced.
The utility model has the advantages of novel design, higher automation degree, lower labor intensity, higher stirring efficiency, higher production efficiency and higher safety factor, is suitable for the emulsification operation of liquid with high viscosity, can ensure that the graphite liquid does not precipitate for a long time after emulsification, can avoid the caking phenomenon before the emulsification of the graphite, has higher working quality and is worthy of popularization and use.
Drawings
Fig. 1 is a schematic structural diagram of a stirring device for graphite liquid production according to the present invention.
Reference numbers in the figures: 1. a base; 2. a support frame; 3. a dry powder stirring tank; 4. a first disperser; 5. a mounting frame; 6. vibrating screen; 7. an auxiliary material stirring tank; 8. a second disperser; 9. a dust collecting pipe; 10. cylinder pulling; 11. an emulsifying machine; 12. an electric hoist; 13. filling the box; 14. a pulse dust collector; 15. a first pneumatic diaphragm pump; 16. a second pneumatic diaphragm pump; 17. a third pneumatic diaphragm pump.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments.
Referring to fig. 1, a stirring device for graphite liquid production comprises a base 1 and a dust collecting pipe 9, wherein a support frame 2, a pull cylinder 10, a filling box 13 and a pulse dust collector 14 are sequentially arranged at the top end of the base 1, a dry powder stirring tank 3, a mounting frame 5 and an auxiliary material stirring tank 7 are sequentially arranged at the top end of the support frame 2, a vibrating screen 6 is arranged at the top end of the mounting frame 5, graphite blocks and sundries which cannot be crushed can be screened out through the vibrating screen 6, a grinding machine is directly omitted, the dust collecting pipe 9 is positioned above the vibrating screen 6, a first disperser 4 is arranged at the top of the dry powder stirring tank 3, a second disperser 8 is arranged at the top of the auxiliary material stirring tank 7, a traditional impeller transposition high-speed disperser is used for realizing quick stirring of graphite powder, the stirring time can be reduced at high rotating speed, the efficiency is improved, a first discharging pipe is arranged at the bottom end of the dry powder stirring tank 3, the bottom end of the first discharging pipe is connected with a first automatic conveying pipe through a first valve, one end of the first conveying pipe, which is far away from the first automatic valve, is connected with a first pneumatic diaphragm pump 15, the discharge end of the first pneumatic diaphragm pump 15 is connected with a vibrating screen 6 through a second conveying pipe, the discharge end of the vibrating screen 6 is connected with a third conveying pipe, the third conveying pipe extends to the inside of an auxiliary material stirring tank 7, the bottom end of the auxiliary material stirring tank 7 is provided with a second discharge pipe, the bottom end of the second discharge pipe is connected with a fourth conveying pipe through a second automatic valve, one end of the fourth conveying pipe, which is far away from the second automatic valve, is connected with a second pneumatic diaphragm pump 16, the discharge end of the second pneumatic diaphragm pump 16 is connected with a fifth conveying pipe, the fifth conveying pipe extends to the inside of a pulling cylinder 10, the top of the pulling cylinder 10 is provided with an emulsifying machine 11, the graphite liquid is fully emulsified and proportioned through the emulsifying machine 11 and then filled, the graphite liquid emulsifying machine is suitable for high-viscosity liquid emulsifying operation, and the graphite liquid can be ensured not to precipitate for a long time after emulsification, the using quality requirement of the perforating machine is not influenced, a third discharging pipe is arranged at the bottom end of the pulling cylinder 10, the side end of the third discharging pipe is connected with a sixth conveying pipe through a third automatic valve, one end, far away from the third automatic valve, of the sixth conveying pipe is connected with a third pneumatic diaphragm pump 17, the discharging end of the third pneumatic diaphragm pump 17 is connected with a seventh conveying pipe, the seventh conveying pipe extends to the inside of the filling box 13, the pneumatic diaphragm pump is used for feeding materials to reduce direct contact graphite, the electric-to-pneumatic operation field is changed into pneumatic operation field to further increase the safety coefficient, the process optimization is adopted, the length of a pipeline from feeding materials to the emulsifying machine 11 is shortened through a short-flow design, and the caking phenomenon before graphite emulsification is further reduced.
The top of dry powder agitator tank 3 is provided with first dust cage, and the top of auxiliary material agitator tank 7 is provided with the second dust cage, and dust collecting pipe 9 is connected with first dust cage through first connecting pipe, and dust collecting pipe 9 is connected with the second dust cage through the second connecting pipe, and dust collecting pipe 9 is connected with pulse dust collector 14 through the third connecting pipe, and the purification is collected to the raise dust realization to accessible dry powder agitator tank 3.
An electric hoist 12 is installed right above the pulling cylinder 10, the output end of the electric hoist 12 is in transmission connection with the pulling cylinder 10, and the pulling cylinder 10 can be driven to move through the work of the electric hoist 12.
When in use, firstly, graphite powder and water are put into the dry powder stirring tank 3, the graphite powder and the water can be quickly and fully stirred and mixed into graphite liquid through the work of the first dispersion machine 4, then, a first automatic valve is opened, the graphite liquid can be conveyed to the vibrating screen 6 through the work of the first pneumatic diaphragm pump 15, graphite blocks and sundries which cannot be broken in the graphite liquid can be screened out through the work of the vibrating screen 6, the graphite liquid is conveyed to the auxiliary material stirring tank 7 through the material conveying pipe, then, ingredients such as antioxidant and the like are put into the auxiliary material stirring tank 7, the ingredients such as the graphite liquid and the antioxidant and the like can be quickly and fully stirred and mixed through the work of the second dispersion machine 8, then, a second automatic diaphragm pump is opened, the stirred graphite liquid can be conveyed to the pull cylinder 10 through the work of the second pneumatic diaphragm pump 16, and then, the work of the emulsifying machine 11 is carried out, can fully emulsify graphite liquid, accomplish the back with graphite liquid emulsification, open the third automatic valve, work through second pneumatic diaphragm pump 16, can carry graphite liquid to filling case 13, can realize the filling of graphite liquid, degree of automation is higher, artifical intensity of labour is lower, stirring efficiency is higher, production efficiency is higher, factor of safety is higher, be applicable to the big liquid emulsification operation of viscosity, can guarantee after the emulsification that graphite liquid does not deposit for a long time, can avoid the caking phenomenon before the graphite emulsification, work quality is higher, be worth using widely.
In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", and the like, indicate orientations and positional relationships based on those shown in the drawings, and are used only for convenience of description and simplicity of description, and do not indicate or imply that the equipment or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be considered as limiting the present invention.
Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless specifically defined otherwise.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the technical scope of the present invention, and equivalent alternatives or modifications according to the technical solution of the present invention and the inventive concept thereof should be covered by the scope of the present invention.
Claims (3)
1. The stirring device for graphite liquid production comprises a base (1) and a dust collecting pipe (9), and is characterized in that a support frame (2), a pulling cylinder (10), a filling box (13) and a pulse dust collector (14) are sequentially arranged on the top end of the base (1), a dry powder stirring tank (3), a mounting frame (5) and an auxiliary material stirring tank (7) are sequentially arranged on the top end of the support frame (2), a vibrating screen (6) is installed on the top end of the mounting frame (5), the dust collecting pipe (9) is positioned above the vibrating screen (6), a first dispersing machine (4) is installed on the top of the dry powder stirring tank (3), a second dispersing machine (8) is installed on the top of the auxiliary material stirring tank (7), a first discharging pipe is arranged at the bottom end of the dry powder stirring tank (3), and a first conveying pipe is connected to the bottom end of the first discharging pipe through a first automatic valve, one end of the first conveying pipe, which is far away from the first automatic valve, is connected with a first pneumatic diaphragm pump (15), the discharge end of the first pneumatic diaphragm pump (15) is connected with a vibrating screen (6) through a second conveying pipe, the discharge end of the vibrating screen (6) is connected with a third conveying pipe, the third conveying pipe extends to the inside of an auxiliary material stirring tank (7), the bottom end of the auxiliary material stirring tank (7) is provided with a second discharge pipe, the bottom end of the second discharge pipe is connected with a fourth conveying pipe through a second automatic valve, one end of the fourth conveying pipe, which is far away from the second automatic valve, is connected with a second pneumatic diaphragm pump (16), the discharge end of the second pneumatic diaphragm pump (16) is connected with a fifth conveying pipe, the fifth conveying pipe extends to the inside of a pulling cylinder (10), the top of the pulling cylinder (10) is provided with an emulsifying machine (11), and the bottom end of the pulling cylinder (10) is provided with a third discharge pipe, the side of the third discharging pipe is connected with a sixth conveying pipe through a third automatic valve, one end, far away from the third automatic valve, of the sixth conveying pipe is connected with a third pneumatic diaphragm pump (17), the discharging end of the third pneumatic diaphragm pump (17) is connected with a seventh conveying pipe, and the seventh conveying pipe extends to the inside of the filling box (13).
2. The stirring device for graphite liquid production according to claim 1, wherein a first dust hood is disposed on the top of the dry powder stirring tank (3), a second dust hood is disposed on the top of the auxiliary material stirring tank (7), the dust collecting pipe (9) is connected to the first dust hood through a first connecting pipe, the dust collecting pipe (9) is connected to the second dust hood through a second connecting pipe, and the dust collecting pipe (9) is connected to the pulse dust collector (14) through a third connecting pipe.
3. The stirring device for graphite liquid production according to claim 1, wherein an electric hoist (12) is mounted right above the pulling cylinder (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121225616.0U CN215586272U (en) | 2021-06-03 | 2021-06-03 | Agitating unit is used in production of graphite liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121225616.0U CN215586272U (en) | 2021-06-03 | 2021-06-03 | Agitating unit is used in production of graphite liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215586272U true CN215586272U (en) | 2022-01-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121225616.0U Active CN215586272U (en) | 2021-06-03 | 2021-06-03 | Agitating unit is used in production of graphite liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215586272U (en) |
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2021
- 2021-06-03 CN CN202121225616.0U patent/CN215586272U/en active Active
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