CN218232613U - Anodic oxidation production line - Google Patents

Anodic oxidation production line Download PDF

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Publication number
CN218232613U
CN218232613U CN202222073860.0U CN202222073860U CN218232613U CN 218232613 U CN218232613 U CN 218232613U CN 202222073860 U CN202222073860 U CN 202222073860U CN 218232613 U CN218232613 U CN 218232613U
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copper sheet
electrolyte
anodic oxidation
line according
bearing frame
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CN202222073860.0U
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Chinese (zh)
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李永涛
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Jiaxing Xiaochuang Electronic Technology Co ltd
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Jiaxing Xiaochuang Electronic Technology Co ltd
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Abstract

The utility model relates to an anodic oxidation field especially involves an anodic oxidation production line, including the electrolyte bath, evenly be provided with a plurality of sliding trays on the inside wall of electrolyte bath, every it is provided with a bearing frame to slide in the sliding tray, bearing frame includes that two baffles and a plurality of connection that the interval set up are two the carrier block of baffle, the top of electrolyte bath is provided with the positive pole copper sheet, the bottom surface and every of electrolyte bath the position that the sliding tray corresponds all is provided with a negative pole copper sheet, the positive pole copper sheet with the negative pole copper sheet all with a battery electric connection. The utility model discloses a setting of baffle, load-bearing frame and connecting block for can make the electrolyte in the electrolyte bath remix through the baffle rises, so that adjust the concentration of electrolyte.

Description

Anodic oxidation production line
Technical Field
The utility model relates to an anodic oxidation field especially involves an anodic oxidation production line.
Background
Anodic oxidation, is the electrochemical oxidation of a metal or alloy. The surface treatment method is commonly used for surface treatment of aluminum and aluminum alloy, and the aluminum alloy form an oxide film on an aluminum product (anode) under the action of corresponding electrolyte and specific process conditions and due to the action of impressed current. Can overcome the defects of surface hardness, abrasion resistance and the like of the aluminum alloy, expand the application range and prolong the service life of the aluminum alloy.
Currently, production lines for anodizing often employ multiple, spaced-apart electrolyte baths to enable simultaneous processing of groups of workpieces by a robot. However, since the anodic oxidation has a requirement on the concentration of the electrolyte, the addition and replacement of the electrolyte in the plurality of electrolyte tanks require the concentration in the electrolyte tanks to be measured one by one, which is very cumbersome. Therefore, there is a need for an improved structure that overcomes the above-mentioned deficiencies.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the defects of the prior art and provide an anodic oxidation production line, which is realized by the following technical scheme:
the utility model provides an anodic oxidation production line, includes the electrolyte bath, evenly be provided with a plurality of sliding trays on the inside wall of electrolyte bath, every it is provided with a bearing frame to slide in the sliding tray, bearing frame includes two baffles and a plurality of connection two that the interval set up the bearing block of baffle, the top of electrolyte bath is provided with the positive pole copper sheet, the bottom surface and every of electrolyte bath the position that the sliding tray corresponds all is provided with a negative pole copper sheet, the positive pole copper sheet with negative pole copper sheet all with a battery electric connection.
In the above technical scheme: the electrolyte tank is used for accommodating electrolyte and is also used as a container for anodic oxidation reaction; the bearing frame is used for supporting a hanging tool for arranging products; the partition plates are used for partitioning the electrolyte tank into a plurality of small tanks and can realize switching; the bearing block is used for bearing a hanging tool for arranging products and has the function of enabling the two partition plates in each bearing frame to move simultaneously; after the hanger is connected, the anode copper sheet, the cathode copper sheet and the battery enable a product soaked in the electrolyte tank to be an anode, so that anodic oxidation is achieved.
The utility model discloses a further set up to: the electrolytic bath is provided with a clamping device in a sliding mode, and the clamping device comprises a portal frame and clamping claws arranged on two side walls of the portal frame in a sliding mode.
In the above technical scheme: the clamping device is used for taking out or immersing the hanger provided with the product from the electrolyte tank; the portal frame is used for realizing horizontal movement; the clamping jaw is used for clamping and is also used for realizing up-and-down movement.
The utility model discloses a further set up to: and the bearing block is provided with a limiting groove.
In the above technical scheme: the limiting groove is used for enabling the hanging tool to be positioned.
The utility model discloses a further set up to: the anode copper sheet is electrically connected with the anode of the battery, and the cathode copper sheet is electrically connected with the cathode of the battery.
The utility model discloses a further set up to: the bottom of the electrolyte tank and the position corresponding to the partition plate are provided with clamping grooves, and the partition plate is clamped with the clamping grooves.
In the above technical scheme: the joint groove is used for limiting the partition plate, and meanwhile, the joint groove enables the partition plate to be better in partition effect with the electrolyte tank after descending.
The utility model discloses a further set up to: the bearing frame is characterized by also comprising a connecting block, and each bearing frame is fixedly connected with the connecting block.
In the above technical scheme: the connecting block is used for connecting all the bearing frames so as to realize synchronous movement.
The utility model discloses a further set up to: the electrolyte tank is characterized in that the front outer side wall and the rear outer side wall of the electrolyte tank are respectively provided with at least one cylinder, the output direction of the cylinders is vertical upwards, and the output ends of the cylinders are fixedly connected with the connecting block.
In the above technical scheme: the cylinder is used for pushing the connecting block, so that the connecting block rises or falls, and then the partition board rises or falls.
The utility model discloses an anodic oxidation production line, compare with prior art:
1. the utility model can mix the electrolyte in the electrolyte tank again by the baffle plate, the bearing frame and the connecting block, so as to adjust the concentration of the electrolyte;
2. the utility model discloses a setting in sliding tray and joint groove for the partition of baffle is effectual.
Drawings
Fig. 1 is a top view of the present invention;
fig. 2 is a side view of the present invention;
fig. 3 is a top view of the electrolytic solution tank of the present invention.
The corresponding part names indicated by the numbers and letters in the drawings: 10-an electrolyte bath; 101-a sliding groove; 102-a clamping groove; 20-a carrier frame; 201-a separator; 202-a carrier block; 202 a-a limiting groove; 30-anode copper sheet; 40-cathode copper sheet; 50-a clamping device; 501, gantry; 502-gripper jaw; 60-connecting blocks; 70-cylinder.
Detailed Description
The embodiments of the present invention will be described in detail below, and this embodiment is implemented on the premise of the technical solution of the present invention, and a detailed implementation manner and a specific operation process are given, but the scope of the present invention is not limited to the following embodiments.
As shown in fig. 1-3, the utility model provides an anodic oxidation production line, including electrolyte bath 10, evenly be provided with a plurality of sliding tray 101 on the inside wall of electrolyte bath 10, every it is provided with a bearing frame 20 to slide in the sliding tray 101, bearing frame 20 includes two baffles 201 and a plurality of connection two that the interval set up the bearer block 202 of baffle 201, the top of electrolyte bath 10 is provided with positive pole copper sheet 30, the bottom surface and every of electrolyte bath 10 the position that sliding tray 101 corresponds all is provided with a negative pole copper sheet 40, positive pole copper sheet 30 with negative pole copper sheet 40 all with a battery electric connection. Preferably, the two opposite inner side walls of the electrolyte tank 10 are provided with sliding grooves 101, and the sliding grooves 101 are in one-to-one correspondence, the side walls of the sliding grooves 101 are in a step shape, and correspondingly, the side surfaces of the partition boards 201 are also in a step shape; each bearing frame 20 comprises two bearing blocks 202; the length of the anode copper sheet 30 is similar to that of the electrolyte tank 10, and after a hanger provided with a product is placed on the bearing block 202, one end of the upper part of the hanger is in contact with the anode copper sheet 30; the number of the cathode copper sheets 40 corresponds to the number of the sliding grooves 101.
As shown in fig. 1-3, the utility model provides an anodic oxidation production line, a clamping device 50 is slidably disposed on the electrolyte tank 10, the clamping device 50 includes a portal frame 501 and a clamping claw 502 slidably disposed on two side walls of the portal frame 501. The gantry 501 is in a shape of' 21274, two outer walls of the electrolyte tank 10 are provided with track blocks which protrude outwards, a horizontal second track is arranged on the track blocks, and the gantry 501 is in sliding connection through the tracks; a vertical second rail is arranged on the gantry 501, and the clamping claw 502 is slidably connected with the gantry 501 through the second rail.
As shown in fig. 1-3, the utility model provides an anodic oxidation production line, a limiting groove 202a is provided on the bearing block 202. Preferably, the limiting groove 202a is disposed in the middle of the bearing block 202, the shape of the limiting groove 202a corresponds to the shape of a hanger for setting a product, and the height of the bottom surface of the limiting groove 202a is consistent with the height of the anode copper sheet 30.
As shown in fig. 1-3, the present invention provides an anodic oxidation production line, the anode copper sheet 30 is electrically connected to the anode of the battery, and the cathode copper sheet 40 is electrically connected to the cathode of the battery.
As shown in fig. 1-3, in the anodic oxidation production line provided by the present invention, a clamping groove 102 is disposed at a position corresponding to the partition plate 201 at the bottom of the electrolyte tank 10, and the partition plate 201 is clamped with the clamping groove 102. The side wall of the electrolyte tank 10 may be provided with a drain hole at a position corresponding to the fastening groove 102, so as to drain water completely.
As shown in fig. 1-3, the anodic oxidation production line of the present invention further includes a connection block 60, and each of the supporting frames 20 is fixedly connected to the connection block 60. Wherein the connecting block 60 is arranged in the structure of the shape of '21274', of the portal frame 501, so as to avoid the interference condition from occurring.
As shown in fig. 1-3, the utility model provides an anodic oxidation production line, respectively be provided with at least one cylinder 70 on the lateral wall around the electrolyte bath 10, the output direction of cylinder 70 is vertical upwards, just the output of cylinder 70 with connecting block 60 fixed connection. Wherein the number of cylinders 70 on each side wall is preferably two.
The utility model discloses a theory of operation does:
a) Adding an electrolyte to the electrolyte cell;
b) The cylinder descends to lead the partition board to partition the electrolyte tank into a plurality of small electrolyte tanks;
c) The hanging tool provided with the product is clamped by a clamping claw of the clamping device;
d) The portal frame moves to the upper part of the small electrolyte tank, the clamping claw descends, and the hanger is put down;
e) One end of the hanger is contacted with the anode copper sheet, and a product at one end is immersed in the electrolyte for anodic oxidation;
f) The portal frame is operated for multiple times, so that the hangers are subjected to anodic oxidation simultaneously;
g) After the anodic oxidation is finished, taking out the anode from the clamping device;
h) After several operations, the concentration in each electrolyte cell may be different;
i) The cylinder rises, the partition plate rises along with the cylinder, and all the electrolyte in each small electrolyte tank is mixed;
j) After the concentration is measured, adding electrolyte according to the measured concentration to ensure that the concentration is qualified again;
k) Repeating a) -j.
Above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the design of the present invention, equivalent replacement or change should be covered within the protection scope of the present invention.
It should be noted that, in this document, relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrases "comprising a," "8230," "8230," or "comprising" does not exclude the presence of additional like elements in a process, method, article, or apparatus that comprises the element.

Claims (7)

1. An anodic oxidation production line comprises an electrolyte tank (10), and is characterized in that: the electrolytic cell is characterized in that a plurality of sliding grooves (101) are uniformly formed in the inner side wall of the electrolytic cell (10), a bearing frame (20) is arranged in each sliding groove (101) in a sliding mode, each bearing frame (20) comprises two partition plates (201) arranged at intervals and a plurality of bearing blocks (202) connected with the two partition plates (201), an anode copper sheet (30) is arranged at the top of the electrolytic cell (10), a cathode copper sheet (40) is arranged at the position, corresponding to each sliding groove (101), of the bottom surface of the electrolytic cell (10), and the anode copper sheet (30) and the cathode copper sheet (40) are electrically connected with a battery.
2. An anodizing line according to claim 1, wherein: the electrolytic solution tank (10) is provided with a clamping device (50) in a sliding mode, and the clamping device (50) comprises a portal frame (501) and clamping claws (502) arranged on two side walls of the portal frame (501) in a sliding mode.
3. An anodizing line according to claim 2, wherein: the bearing block (202) is provided with a limiting groove (202 a).
4. An anodizing line according to claim 3, wherein: the anode copper sheet (30) is electrically connected with the anode of the battery, and the cathode copper sheet (40) is electrically connected with the cathode of the battery.
5. An anodizing line according to claim 4, wherein: the bottom of electrolyte bath (10) with the position that baffle (201) corresponds is provided with joint groove (102), baffle (201) with joint groove (102) joint.
6. An anodizing line according to claim 1 or 5, wherein: the device also comprises a connecting block (60), and each bearing frame (20) is fixedly connected with the connecting block (60).
7. An anodizing line according to claim 6, wherein: the front outer side wall and the rear outer side wall of the electrolyte tank (10) are respectively provided with at least one air cylinder (70), the output direction of the air cylinders (70) is vertical and upward, and the output ends of the air cylinders (70) are fixedly connected with the connecting blocks (60).
CN202222073860.0U 2022-08-08 2022-08-08 Anodic oxidation production line Active CN218232613U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202222073860.0U CN218232613U (en) 2022-08-08 2022-08-08 Anodic oxidation production line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202222073860.0U CN218232613U (en) 2022-08-08 2022-08-08 Anodic oxidation production line

Publications (1)

Publication Number Publication Date
CN218232613U true CN218232613U (en) 2023-01-06

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202222073860.0U Active CN218232613U (en) 2022-08-08 2022-08-08 Anodic oxidation production line

Country Status (1)

Country Link
CN (1) CN218232613U (en)

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