CN209773001U

CN209773001U - Graphite deacidification tank

Info

Publication number: CN209773001U
Application number: CN201920032957.2U
Authority: CN
Inventors: 刘洪法
Original assignee: Qingdao Middle East Graphite Co Ltd
Current assignee: Qingdao Middle East Graphite Co Ltd
Priority date: 2019-01-09
Filing date: 2019-01-09
Publication date: 2019-12-13
Anticipated expiration: 2029-01-09

Abstract

The utility model relates to a graphite deacidification tank, which belongs to the technical field of graphite processing equipment, and the key point of the technical scheme is that the graphite deacidification tank comprises a tank body, wherein a partition plate is arranged in the tank body, and the inside of the tank body is divided into an upper material chamber and a lower liquid collecting chamber by the partition plate; be provided with on the division board and run through the division board hole of permeating water, the upper surface of division board covers has the film that permeates water, its characterized in that: the separation plate is rotatably connected with the tank body around a horizontal axis, the liquid collection chamber is provided with a material receiving disc, the material receiving disc is connected with the tank body in a sliding mode along the horizontal direction, and one side of the liquid collection chamber is provided with a discharge hole for drawing the material receiving disc out of the liquid collection chamber; the problem that the graphite powder is inconvenient to take out of the tank body after deacidification is finished by adopting the conventional graphite deacidification tank to deacidify the graphite powder is solved; the deacidified graphite powder can be conveniently and quickly taken out from the tank body.

Description

Graphite deacidification tank

Technical Field

The utility model belongs to the technical field of graphite processing equipment technique and specifically relates to a graphite deacidification jar is related to.

Background

In the solid processing and production process of graphite, the processed graphite powder needs to be subjected to acid washing, so that metal impurities in the graphite powder are removed, and the purity of the graphite powder is improved. After the graphite powder is subjected to acid cleaning, the graphite powder needs to be subjected to water cleaning and deacidification, so that residual acidic substances in the graphite powder are removed.

the existing graphite deacidification tank comprises a tank body, wherein a partition plate fixedly connected with the tank body is arranged in the tank body, and the inside of the tank body is divided into an upper material chamber and a lower liquid collecting chamber by the partition plate; the division plate is provided with a permeable hole penetrating through the division plate, and the upper surface of the division plate is covered with a permeable film. When the graphite deacidification tank is used for deacidifying the graphite powder, the graphite powder is added into the material chamber, water flow is introduced into the graphite powder, and then the graphite in the material chamber is cleaned by the water flow, so that acidic substances in the graphite powder are removed. The waste water that carries the acid material enters into the collecting chamber through the film that permeates water by the hole of permeating water, and then realizes the deacidification washing to graphite powder, after accomplishing the deacidification to graphite powder, takes out graphite powder from jar internal, carries out the processing of next process again.

Graphite powder is powdered solid, adopts current graphite deacidification jar to carry out the deacidification to graphite powder, accomplishes the deacidification back, takes out graphite powder from jar internal inconvenience.

SUMMERY OF THE UTILITY MODEL

The utility model aims at providing a graphite deacidification jar, can convenient and fast take out graphite powder after the deacidification from jar internal.

The above utility model discloses an above-mentioned utility model purpose can realize through following technical scheme: a graphite deacidification tank comprises a tank body, wherein a partition plate is arranged in the tank body, and divides the interior of the tank body into an upper material chamber and a lower liquid collecting chamber; the improved liquid collecting tank is characterized in that a permeable hole penetrating through the partition plate is formed in the partition plate, a permeable film covers the upper surface of the partition plate, the partition plate is connected with the tank body in a rotating mode around a horizontal axis, the liquid collecting chamber is provided with a material receiving disc, the material receiving disc is connected with the tank body in a sliding mode along the horizontal direction, and a discharge hole for taking the material receiving disc out of the liquid collecting chamber is formed in one side of the liquid collecting chamber.

by adopting the technical scheme, the partition plate is rotatably connected with the tank body around the horizontal axis, the liquid collection chamber is provided with the material receiving disc, the material receiving disc is connected with the tank body in a sliding manner along the horizontal direction, and one side of the liquid collection chamber is provided with a discharge hole for drawing the material receiving disc out of the liquid collection chamber; when carrying out the washing deacidification to the graphite powder in the material room, take the take-up (stock) pan out from collecting the liquid room, through rotating the division board around its articulated shaft in accomplishing the material room, and then empty the graphite powder in the material room on the take-up (stock) pan, take the take-up (stock) pan out from the discharge gate to convenient and fast takes out the graphite powder from jar internal.

The utility model discloses further set up to: and a collecting hopper with the cross section gradually reduced from top to bottom is arranged in the liquid collecting chamber above the material receiving disc, and the collecting hopper is fixedly connected with the tank body.

Through adopting above-mentioned technical scheme, be provided with in the collection liquid chamber of take-up (stock) pan top by the upper to lower cross section reduce gradually gather the hopper, gather hopper and jar body fixed connection to accept the graphite powder that falls down in the material chamber, and then gather the graphite powder in the take-up (stock) pan middle part.

The utility model discloses further set up to: the division board is fixed with the horizontally pivot, the pivot is connected with jar rotation around its axis, the one end of pivot is provided with driving motor, driving motor's organism and jar body fixed connection, driving motor's output shaft and the coaxial setting of pivot and with pivot fixed connection.

Through adopting above-mentioned technical scheme, the division board is fixed with the horizontally pivot, the pivot is rotated around its axis and jar and is connected, the one end of pivot is provided with driving motor, driving motor's organism and jar body fixed connection, driving motor's output shaft and the coaxial setting of pivot and with pivot fixed connection, rotate around its axis through driving motor drive pivot to convenient and fast overturns the division board, and then pours the graphite powder in the material room into the take-up (stock) pan.

The utility model discloses further set up to: the filter plate is characterized in that filter holes penetrating through the plate bottom of the material receiving plate are formed in the plate bottom of the material receiving plate, and a water permeable film covers the upper surface of the plate bottom of the material receiving plate.

through adopting above-mentioned technical scheme, be provided with the filtration pore that runs through take-up dish bottom of trying to get to the dish bottom upper surface at take-up dish covers there is the film that permeates water, thereby when carrying out the washing deacidification to graphite powder, can not take out take-up dish from collecting the liquid room, convenient operation, and the moisture in the graphite powder that falls to take-up dish can fall to the collecting the liquid room of take-up dish below through permeating water film and filtration pore, thereby reduce the moisture in the graphite powder that takes out from the jar body.

The utility model discloses further set up to: still include to jar body opening carry out the lid that seals.

Through adopting above-mentioned technical scheme, contain the acid material and when the graphite powder is not washing, can give out acid gas to air on every side, and then produce pungent smell, seal jar body opening through the lid to improve the operational environment when the staff carries out the deacidification to the graphite powder.

The utility model discloses further set up to: one end of the cover body is hinged to the tank body in the horizontal axial direction, the opening and closing cylinders are arranged on the two sides of the cover body, the cylinder body of each opening and closing cylinder is hinged to the tank body in the horizontal axis direction, and the piston rod of each opening and closing cylinder is hinged to the cover body in the horizontal axis direction.

Through adopting above-mentioned technical scheme, lid one end is articulated with a jar body around horizontal axial, and the both sides of lid are provided with opens and close the cylinder, and the cylinder body of opening and close the cylinder is articulated around horizontal axis and jar body, and the piston rod of opening and close the cylinder is articulated around horizontal axis and lid, and the piston rod through opening and close the cylinder contracts to the drive lid rotates around its articulated shaft, thereby convenient and fast opens or is closed with the lid.

The utility model discloses further set up to: the liquid collection chamber is communicated with a negative pressure pipe, and the negative pressure pipe is connected with a negative pressure fan.

Through adopting above-mentioned technical scheme, the collecting chamber intercommunication has the negative pressure pipe, and the negative pressure union coupling has negative pressure fan, accomplishes the washing deacidification to graphite powder after, bleeds to the collecting chamber through negative pressure fan to make the collecting chamber be in the negative pressure state, and then make the moisture in the graphite powder break away from with the graphite powder easily and enter into in the collecting chamber.

The utility model discloses further set up to: the liquid collecting chamber is communicated with a liquid discharge pipe, and the height of the communication position of the liquid discharge pipe is lower than that of the communication position of the negative pressure pipe; and a switch valve for controlling the communication of the liquid discharge pipe is arranged on the liquid discharge pipe.

By adopting the technical scheme, the liquid collecting chamber is communicated with the liquid discharge pipe, and the height of the communication position of the liquid discharge pipe is lower than that of the communication position of the negative pressure pipe; the liquid discharge pipe is provided with a switch valve for controlling the liquid discharge pipe to be communicated, so that liquid in the liquid collection chamber can be conveniently and quickly discharged by opening the switch valve.

To sum up, the utility model discloses a beneficial technological effect does:

1. The partition plate is rotatably connected with the tank body around a horizontal axis, the liquid collecting chamber is provided with a material receiving disc, the material receiving disc is connected with the tank body in a sliding mode along the horizontal direction, and one side of the liquid collecting chamber is provided with a discharge hole for drawing the material receiving disc out of the liquid collecting chamber; when the graphite powder in the material chamber is washed with water for deacidification, the material receiving disc is drawn out from the liquid collecting chamber, and the partition plate rotates around the hinge shaft of the partition plate in the material chamber, so that the graphite powder in the material chamber is poured on the material receiving disc, and the material receiving disc is drawn out from the discharge port, and therefore the graphite powder can be conveniently and quickly taken out of the tank body;

2. the graphite deacidification tank also comprises a cover body for sealing the opening of the tank body, one end of the cover body is hinged with the tank body around the horizontal axial direction, opening and closing cylinders are arranged on two sides of the cover body, a cylinder body of each opening and closing cylinder is hinged with the tank body around the horizontal axial line, a piston rod of each opening and closing cylinder is hinged with the cover body around the horizontal axial line, and the cover body is driven to rotate around a hinged shaft of the cover body through contraction of the piston rod of each opening and closing cylinder, so that the opening of the tank body is conveniently and quickly sealed, the emission of acid gas to the outside is reduced, and the working;

3. The liquid collection chamber is communicated with a negative pressure pipe, the negative pressure pipe is connected with a negative pressure fan, and the negative pressure fan is used for exhausting air to the liquid collection chamber, so that the liquid collection chamber is in a negative pressure state, and further, moisture in the graphite powder is easily separated from the graphite powder and enters the liquid collection chamber, and the moisture in the deacidified graphite is reduced.

Drawings

FIG. 1 is a schematic structural diagram of a graphite deacidification tank;

FIG. 2 is a sectional view showing the internal structure of the can body;

FIG. 3 is a schematic view of the structure of the partition plate;

Fig. 4 is a schematic structural diagram of the take-up pan.

In the figure, 1, a tank body; 11. a partition plate; 111. water permeable holes; 112. a rotating shaft; 113. a drive motor; 12. a material chamber; 121. a water inlet pipe; 13. a liquid collection chamber; 131. a negative pressure tube; 132. a negative pressure fan; 133. a liquid discharge pipe; 134. an on-off valve; 14. a discharge port; 2. a cover body; 21. opening and closing the air cylinder; 3. a water permeable film; 4. a take-up pan; 41. filtering holes; 5. a gathering hopper.

Detailed Description

The present invention will be described in further detail with reference to the accompanying drawings.

Referring to fig. 1 and 2, a graphite deacidification tank comprises a tank body 1, wherein a partition plate 11 is arranged in the tank body 1, and the partition plate 11 divides the interior of the tank body 1 into an upper material chamber 12 and a lower liquid collecting chamber 13. The material chamber 12 is communicated with a water inlet pipe 121. The drain pipe 133 is connected to the drain chamber 13, and the drain pipe 133 is provided with an on-off valve 134 for controlling the connection of the drain pipe 133. The partition plate 11 is provided with water permeable holes 111 penetrating through the partition plate 11, and the upper surface of the partition plate 11 is covered with a water permeable film 3. The upper part of the tank body 1 is provided with a cover body 2 for sealing the opening of the tank body 1. Lid 2 one end is articulated with jar body 1 around horizontal axial, and the both sides of lid 2 are provided with opens and close cylinder 21, and the cylinder body of opening and close cylinder 21 is articulated with jar body 1 around horizontal axis, and the piston rod of opening and close cylinder 21 is articulated with lid 2 around horizontal axis. After the graphite powder to be deacidified is added into the material chamber 12, the cover body 2 is driven to be closed by the opening and closing cylinder 21, so that the dispersion of acid gas in the air is reduced when the graphite powder is deacidified. Through the rivers that go into in to material chamber 12 through inlet tube 121, and then carry out the washing through rivers to the graphite powder in the material chamber 12, the rivers of wasing graphite enter into the collection liquid chamber 13 of lower part through the film 3 that permeates water and the hole 111 that permeates water to accomplish the deacidification to the graphite powder. By opening the on-off valve 134, the wastewater after the deacidification treatment is discharged from the liquid collecting chamber 13.

Referring to fig. 2, the liquid collection chamber 13 is further communicated with a negative pressure pipe 131, the negative pressure pipe 131 is connected with a negative pressure fan 132, the height of the communication position of the liquid discharge pipe 133 is lower than that of the communication position of the negative pressure pipe 131, and when deacidifying and washing the graphite powder, the negative pressure fan 132 is used for sucking air into the liquid collection chamber 13, so that the liquid collection chamber 13 is in a negative pressure state, and further, moisture in the graphite powder is easily separated from the graphite powder and enters the liquid collection chamber 13, and moisture in the deacidified graphite is reduced.

Referring to fig. 2 and 3, a horizontal rotating shaft 112 is fixed to the partition plate 11, and the rotating shaft 112 is rotatably connected to the tank 1 around the axis thereof. One end of the rotating shaft 112 is provided with a driving motor 113, the body of the driving motor 113 is fixedly connected with the tank body 1, and the output shaft of the driving motor 113 is coaxially arranged with the rotating shaft 112 and fixedly connected with the rotating shaft 112.

Referring to fig. 2 and 4, the liquid collecting chamber 13 is provided with a material receiving disc 4, the bottom of the material receiving disc 4 is provided with filter holes 41 penetrating through the bottom of the material receiving disc 4, and the upper surface of the bottom of the material receiving disc 4 is covered with a water permeable film 3. The material receiving disc 4 is connected with the tank body 1 in a sliding mode along the horizontal direction, and a discharge hole 14 for drawing the material receiving disc 4 out of the liquid collecting chamber 13 is formed in one side of the liquid collecting chamber 13. When the graphite powder is washed with water for deacidification, wastewater after deacidification enters the liquid collecting chamber 13 and enters the liquid collecting chamber 13 below the material receiving disc 4 through the permeable film 3 on the material receiving disc 4 and the filter holes 41 on the material receiving disc 4. After the graphite powder is washed and cleaned, the driving motor 113 drives the rotating shaft 112 to rotate around the axis of the rotating shaft, and then the material in the material chamber 12 is poured onto the material receiving plate 4. The receiving disc 4 is drawn out from the discharge hole 14, so that the graphite powder after being washed and cleaned can be conveniently and quickly taken out from the tank body 1.

referring to fig. 2, a collecting hopper 5 with a cross section gradually reduced from top to bottom is arranged in a liquid collecting chamber 13 above the material receiving disc 4, and the collecting hopper 5 is fixedly connected with the tank body 1. Through the setting of gathering hopper 5, accept the graphite powder that falls in the material room 12, and then gather the graphite powder in take-up (stock) pan 4 middle part.

The implementation principle of the embodiment is as follows:

graphite powder to be deacidified is added into the material chamber 12, and the cover body 2 is driven to be closed by the driving motor 113. Through going into rivers in to material chamber 12 through inlet tube 121, and then carry out the washing through rivers to the graphite powder in the material chamber 12, the rivers that wash graphite enter into the collecting chamber 13 of lower part through the film 3 that permeates water and the hole 111 that permeates water, and then enter into the collecting chamber 13 of collecting tray 4 below through collecting tray 4. After the deacidification cleaning of the graphite powder is completed, the negative pressure fan 132 is used for pumping the liquid collection chamber 13 through the negative pressure fan 132, so that the liquid collection chamber 13 is in a negative pressure state, the moisture in the graphite powder is easily separated from the graphite powder and enters the liquid collection chamber 13, and the moisture in the deacidified graphite is reduced. After the graphite powder is dehydrated, the rotating shaft 112 is driven to rotate by the driving motor 113, so that the graphite powder in the material chamber 12 is poured into the liquid collecting chamber 13, and the graphite powder entering the liquid collecting chamber 13 falls onto the material receiving disc 4 through the material gathering of the material gathering hopper 5. The material receiving disc 4 is pulled out from the material receiving opening, so that the deacidified graphite powder can be conveniently and quickly taken out from the tank body 1.

the embodiment of this specific implementation mode is the preferred embodiment of the present invention, not limit according to this the utility model discloses a protection scope, so: all equivalent changes made according to the structure, shape and principle of the utility model are covered within the protection scope of the utility model.

Claims

1. A graphite deacidification tank comprises a tank body (1), wherein a partition plate (11) is arranged in the tank body (1), and the partition plate (11) divides the interior of the tank body (1) into an upper material chamber (12) and a lower liquid collecting chamber (13); be provided with on division board (11) and run through division board (11) hole (111) of permeating water, the upper surface of division board (11) covers and has permeable film (3), its characterized in that: division board (11) are connected with jar body (1) rotation around horizontal axis, collection liquid chamber (13) are provided with take-up (4), take-up (4) along horizontal direction and jar body (1) sliding connection, discharge gate (14) of collecting liquid chamber (13) are taken out to take-up (4) are seted up to one side of collection liquid chamber (13).

2. The graphite deacidification tank according to claim 1, wherein: a collecting hopper (5) with the cross section gradually reduced from top to bottom is arranged in a liquid collecting chamber (13) above the material receiving disc (4), and the collecting hopper (5) is fixedly connected with the tank body (1).

3. The graphite deacidification tank according to claim 1, wherein: division board (11) are fixed with horizontally pivot (112), pivot (112) are connected with the jar rotation around its axis, the one end of pivot (112) is provided with driving motor (113), the organism and the jar body (1) fixed connection of driving motor (113), the output shaft and the coaxial setting of pivot (112) of driving motor (113) and with pivot (112) fixed connection.

4. The graphite deacidification tank according to claim 1, wherein: the filter disc is characterized in that filter holes (41) penetrating through the disc bottom of the receiving disc (4) are formed in the disc bottom of the receiving disc (4), and a permeable film (3) covers the upper surface of the disc bottom of the receiving disc (4).

5. The graphite deacidification tank according to claim 1, wherein: the tank also comprises a cover body (2) for sealing the opening of the tank body (1).

6. The graphite deacidification tank according to claim 5, wherein: the utility model discloses a jar body, including lid (2), horizontal axis is articulated with jar body (1) around lid one end, the both sides of lid (2) are provided with opens and close cylinder (21), the cylinder body of opening and close cylinder (21) is articulated with jar body (1) around horizontal axis, the piston rod of opening and close cylinder (21) is articulated with lid (2) around horizontal axis.

7. The graphite deacidification tank according to claim 4, wherein: the liquid collection chamber (13) is communicated with a negative pressure pipe (131), and the negative pressure pipe (131) is connected with a negative pressure fan (132).

8. The graphite deacidification tank according to claim 7, wherein: the liquid collecting chamber (13) is communicated with a liquid discharge pipe (133), and the height of the communication position of the liquid discharge pipe (133) is lower than that of the communication position of the negative pressure pipe (131); the liquid discharge pipe (133) is provided with a switch valve (134) for controlling the communication of the liquid discharge pipe (133).