CN212741558U - Directional guide plate of anode tank and foil forming machine - Google Patents
Directional guide plate of anode tank and foil forming machine Download PDFInfo
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- CN212741558U CN212741558U CN202021477321.8U CN202021477321U CN212741558U CN 212741558 U CN212741558 U CN 212741558U CN 202021477321 U CN202021477321 U CN 202021477321U CN 212741558 U CN212741558 U CN 212741558U
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Abstract
The utility model discloses an anode tank directional guide plate and a foil forming machine, which comprises a connecting end and a guide end, wherein the connecting end is arranged below the guide end, two ends of the guide end are bent downwards, and two ends of the guide end are butted with two sides of an opening above an anode tank inlet; strip-shaped diversion through grooves are symmetrically formed in two sides of the surface of the diversion end. Through setting up the water conservancy diversion end and having seted up strip water conservancy diversion logical groove, make electrolyte pass through strip water conservancy diversion logical groove and evenly flow to both sides, reinforcing the directionality of flowing, solved because the non-uniform non-directional that flows, lead to local area's copper ion to distribute inhomogeneous, produce the problem that the scorching phenomenon influences copper foil production quality. The both ends of the flow guide end are bent downwards, and the two ends of the flow guide end are abutted to the upper opening of the liquid inlet of the anode tank, and the flow guide through groove formed in the radial direction of the flow guide end is matched, so that the electrolyte can only flow out from the flow guide through groove, the flowing direction of the electrolyte is ensured to be locked to flow towards the two sides of the anode tank, and the problem that bubbles are increased due to the turbulent flow and the offset of the electrolyte in the anode tank is solved.
Description
Technical Field
The utility model discloses be applied to, specifically be a directional guide plate of anode trough and crude foil machine.
Background
At present, copper foil is an indispensable important basic material in the electronic industry, and particularly, as the new energy industry is further upgraded, the 6 μm or less electrolytic copper foil has wider market prospect, and the quality requirement on the 6 μm or less electrolytic copper foil is higher and higher. Adopt the mode of pouring into the positive pole groove with electrolyte to carry out the technology of electrolytic manufacturing in the manufacturing process, current operation mode does, directly rush into the positive pole inslot through the positive pole groove inlet with electrolyte, has following technical problem:
1. the electrolyte directly impacts the titanium roller for a long time to cause abrasion damage of the titanium roller, and sputtering occurs after the titanium roller is impacted to cause local electrolyte impact to generate a large amount of bubbles with larger volume, so that the production quality of the copper foil is seriously influenced.
2. The flowing of the electrolyte is uneven and non-directional, so that the copper ions in a local area are unevenly distributed, and the scorching phenomenon is generated to influence the production quality of the copper foil.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that the prior art is not enough, a directional guide plate of anode tank and foil forming machine are provided.
In order to solve the technical problem, the anode slot directional guide plate of the utility model is arranged at the inlet of the anode slot, and comprises a connecting end with a rectangular cross section and a guide end with an arc cross section, wherein the connecting end is arranged below the guide end, two ends of the guide end with the arc cross section are bent downwards, and two ends of the guide end are butted with two sides of an opening above the inlet of the anode slot;
strip-shaped flow guide through grooves are symmetrically formed in two sides of the surface of the flow guide end.
As a possible implementation manner, further, a plurality of groups of shunting guide plates for uniformly shunting the electrolyte are symmetrically arranged on the side walls of the two sides of the liquid inlet of the anode tank at intervals, and the connecting ends are welded on the shunting guide plates on the two sides.
As a preferred option, it is preferred that the connecting end and the flow guiding end are of an integrated structure.
As a preferred option, the length of the connecting end and the flow guiding end is preferably 0.8-1.2 m.
As a possible implementation manner, further, the strip-shaped diversion through groove is formed along the radial direction of the diversion end with the arc-shaped cross section.
The green foil machine comprises the anode tank directional guide plate.
The utility model adopts the above technical scheme, following beneficial effect has:
1. the utility model discloses install in the positive pole groove inlet, the electrolyte of dashing into the positive pole groove is shunted, prevents that the long-term high-speed direct impact titanium roller of electrolyte from leading to the wearing and tearing of titanium roller to damage.
2. The utility model discloses a set up the water conservancy diversion end and seted up strip water conservancy diversion and lead to the groove for electrolyte is through the water conservancy diversion that strip water conservancy diversion led to the groove to both sides uniform flow down, has strengthened the directionality that electrolyte flows, has solved because the inhomogeneous non-directionality of flow of electrolyte, and the copper ion that leads to local area distributes inhomogeneously, produces the problem that the phenomenon of scorching influences copper foil production quality. The both ends of the flow guide end are bent downwards, and the two ends of the flow guide end are matched with the flow guide through grooves formed in the radial direction of the flow guide end with the arc-shaped cross section along the butt joint of the two sides of the upper opening of the liquid inlet of the anode groove, so that electrolyte can only flow out of the flow guide through grooves, the flowing direction of the electrolyte is ensured to be locked to flow towards the two sides of the anode groove, and the problem that bubbles are increased due to the turbulent flow and the offset in the anode groove is solved.
Drawings
The present invention will be described in further detail with reference to the following drawings and embodiments:
FIG. 1 is a schematic view of the installation position of the present invention;
FIG. 2 is a side view of the structure of the present invention;
FIG. 3 is a schematic perspective view of the present invention;
FIG. 4 is a schematic view of the connection position of the connection end and the diversion guide plate of the present invention;
fig. 5 is a top view of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the drawings of the embodiments of the present invention will be combined to clearly and completely describe the technical solutions of the embodiments of the present invention.
As shown in fig. 1-5, the utility model provides an anode tank directional guide plate, which is installed at the inlet of an anode tank 1, and comprises a connecting end 2 with a rectangular cross section and a guide end 3 with an arc cross section, wherein the connecting end 2 is arranged below the guide end 3, two ends of the guide end 3 with the arc cross section are bent downwards, and two ends of the guide end are abutted against two sides of the opening above the inlet of the anode tank 1;
strip-shaped flow guide through grooves 301 are symmetrically formed in two sides of the surface of the flow guide end 3.
As a possible implementation manner, further, a plurality of groups of shunting guide plates 101 for uniformly shunting the electrolyte are symmetrically arranged on the side walls of both sides of the liquid inlet of the anode tank 1 at intervals, and the connecting end 2 is welded on the shunting guide plates 101 of both sides.
As a preferred option, the connection end 2 and the diversion end 3 are preferably of an integrated structure.
As a preferred option, the length of the connecting end 2 and the flow guiding end 3 is preferably 0.8-1.2 m.
As a possible implementation manner, further, the strip-shaped diversion through groove 301 is opened along the radial direction of the diversion end 3 with the arc-shaped cross section.
The green foil machine comprises the anode tank directional guide plate.
In the electrolyte input process, electrolyte upwards inputs along the reposition of redundant personnel deflector 101 of 1 inlet both sides in anode tank, and electrolyte strikes link 2 and water conservancy diversion end 3, has replaced the feed liquor mode of the titanium roller of direct impact anode tank in 1 in the traditional handicraft, effectively prevents that the long-term high-speed direct impact titanium roller of electrolyte from leading to the wearing and tearing of titanium roller to damage. Under the shunting of link 2 and water conservancy diversion end 3, ascending electrolyte is along 3 both sides of water conservancy diversion end along the strip water conservancy diversion logical groove 301 blowout that the cross-section was seted up for curved water conservancy diversion end 3 radial direction of water conservancy diversion end for the even directional positive pole groove jet current to both sides of electrolyte, has strengthened the orientation that the electrolyte flows, has solved because the flow of electrolyte is inhomogeneous non-directional, leads to local area's copper ion to distribute inhomogeneous, produces the problem that scorching phenomenon influences copper foil production quality. 3 both ends of water conservancy diversion end are the downwarping, and its both ends lead to the groove 301 along the water conservancy diversion that the cross-section was seted up for curved water conservancy diversion end 3 radial direction with the cooperation of 1 inlet top opening both sides butt in anode tank for electrolyte can only follow water conservancy diversion and lead to the groove 301 outflow, has guaranteed that the direction that electrolyte flows is locked for flowing to 1 both sides in anode tank, prevents that electrolyte from appearing the indiscriminate flow offset in anode tank 1 and leading to the bubble to increase the scheduling problem.
The above embodiments are the embodiments of the present invention, and for those skilled in the art, according to the teaching of the present invention, the equivalent changes, modifications, replacements and variations made by the claims of the present invention should all belong to the scope of the present invention without departing from the principle and spirit of the present invention.
Claims (6)
1. The utility model provides an anode slot directional guide plate, installs in anode slot inlet, its characterized in that: the anode tank comprises a connecting end with a rectangular cross section and a flow guide end with an arc cross section, wherein the connecting end is arranged below the flow guide end, two ends of the flow guide end with the arc cross section are bent downwards, and two ends of the flow guide end are abutted against two sides of an opening above a liquid inlet of an anode tank;
strip-shaped flow guide through grooves are symmetrically formed in two sides of the surface of the flow guide end.
2. The anode cell directional baffle according to claim 1, wherein: the anode tank inlet both sides lateral wall symmetry interval is provided with the reposition of redundant personnel deflector that the multiunit is used for carrying out even reposition of redundant personnel to electrolyte, the link welds on both sides reposition of redundant personnel deflector.
3. The anode cell directional baffle according to claim 1, wherein: the connecting end and the flow guide end are of an integrated structure.
4. The anode cell directional baffle according to claim 1, wherein: the length of the connecting end and the flow guide end is 0.8-1.2 m.
5. The anode cell directional baffle according to claim 1, wherein: the strip-shaped flow guide through groove is formed along the radial direction of the flow guide end with the arc-shaped cross section.
6. A green foil machine characterized by: comprising an anode cell directional baffle according to any one of claims 1 to 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021477321.8U CN212741558U (en) | 2020-07-23 | 2020-07-23 | Directional guide plate of anode tank and foil forming machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021477321.8U CN212741558U (en) | 2020-07-23 | 2020-07-23 | Directional guide plate of anode tank and foil forming machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212741558U true CN212741558U (en) | 2021-03-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021477321.8U Active CN212741558U (en) | 2020-07-23 | 2020-07-23 | Directional guide plate of anode tank and foil forming machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212741558U (en) |
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2020
- 2020-07-23 CN CN202021477321.8U patent/CN212741558U/en active Active
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