CN217839164U - Foil generation device with multiple additive adding ports - Google Patents

Abstract

The utility model relates to a living paper tinsel device with many additives add mouth, include the positive pole unit of being connected with the positive pole electricity, the negative pole roller of being connected with the negative pole electricity, the positive pole unit contains convex quick-witted groove, the radial central axis in convex quick-witted groove is provided with the feed liquor notch, be provided with the polylith anode plate along feed liquor notch left and right sides to convex quick-witted groove both sides upper end radial order respectively, the clearance that sets up between negative pole roller and all anode plates forms the anode slot, the feed liquor notch both sides that convex quick-witted groove lies in all are provided with the second grade inlet of the rectangular slit structure in a plurality of intercommunication anode slots, second grade inlet and feed liquor notch are respectively through corresponding solution pump connection external corresponding solution tank. The utility model discloses a set up the second grade inlet of a plurality of rectangular slit structures in order to supply the additive to regulate and control the concentration homogeneity of whole convex quick-witted inslot solution, make the solution concentration and the inlet tank mouth of convex quick-witted groove both sides tend to be close, improve copper foil length direction's thickness homogeneity.

Description

Foil generation device with multiple additive adding ports

Technical Field

The utility model relates to a raw foil apparatus for producing specifically indicates a raw foil device with many additives add mouthful.

Background

At present, copper foil is an indispensable important basic material in the electronic industry, and particularly, with the further upgrading of the new energy industry, the electrolytic copper foil is produced by plating copper crystal grains on the surface of a part soaked by flowing copper sulfate solution by a cathode roller according to the electroplating principle. The liquid inlet of the traditional anode unit is arranged below the center of the arc-shaped machine groove, along with the generation of solution electrolytic copper foil, the electrolyzed solution is discharged from the liquid outlet at the upper end, and the solution is continuously supplemented and added at the position of the liquid inlet, so that the concentration at the position is higher than the concentration at two sides, particularly the two top ends of the arc-shaped machine groove, and the copper foil in the length direction is uneven. Therefore, the present invention has been made to solve the above-mentioned problems and an object of the present invention is to provide a novel and improved structure.

SUMMERY OF THE UTILITY MODEL

To the problem that above-mentioned prior art exists, the utility model aims to provide a raw paper tinsel device with many additives add mouthful, this raw paper tinsel device with many additives add mouthful can effectively solve the problem that above-mentioned prior art exists.

The technical scheme of the utility model is that:

the utility model provides a give birth to paper tinsel device with many additives interpolation mouth, includes the positive pole unit of being connected with the positive electricity, the negative pole roller of being connected with the negative electricity, the positive pole unit contains convex quick-witted groove, the radial central axis in convex quick-witted groove is provided with the feed liquor notch, is provided with the polylith anode plate along feed liquor notch left and right sides to convex quick-witted groove both sides upper end radial order respectively, the clearance that sets up between negative pole roller and all anode plates forms the anode tank, convex quick-witted groove in the both sides of feed liquor notch all be provided with a plurality of intercommunications the second grade inlet of anode tank, the second grade inlet is rectangular slit structure, external corresponding solution tank is connected through corresponding solution pump respectively to second grade inlet and rectangular shape feed liquor notch.

The splicing surface of the anode plate is an inclined surface which inclines upwards.

The secondary liquid inlet is arranged at the position of the arc-shaped machine groove between the connecting gaps of the adjacent anode plates.

The second-stage liquid inlet is divided into a plurality of flow guide channels by corresponding partition plates, and each liquid inlet flow guide channel is connected with the solution pump through a corresponding metering valve and a multi-way pipe.

The width of the flow guide channel is 1-5 mm.

The caliber of the secondary liquid inlet along the two sides of the arc-shaped machine groove is gradually increased, and the maximum caliber is smaller than that of the liquid inlet groove.

The upper end position of the inner arc surface of the circular arc machine groove and the upper side of the topmost anode plate are provided with a liquid outlet, the liquid outlet is communicated with a liquid drainage channel embedded in the circular arc machine groove, and an outlet of the liquid drainage channel is arranged on the outer arc surface outer side of the circular arc machine groove and is downward in opening.

The utility model has the advantages that:

the utility model adds a plurality of strip slit secondary liquid inlets to supplement additives, thereby regulating the concentration uniformity of the dissolved liquid in the whole arc machine groove, leading the dissolved liquid concentration on the two sides of the arc machine groove to be close to the liquid inlet notch, and improving the thickness uniformity of the copper foil in the length direction; and the brightening agent is added into the additive of the secondary liquid inlet, and the rough surface of the copper foil is fine in grain, so that the high-quality copper foil is produced. The caliber of the secondary liquid inlet along the two sides of the circular arc-shaped machine groove is gradually increased, and the maximum caliber is smaller than that of the liquid inlet groove, so that the uniformity of the solution is further adjusted.

Drawings

Fig. 1 is a schematic structural diagram of a foil generating apparatus according to an embodiment of the present invention.

Fig. 2 is a schematic structural diagram of an anode plate with a thickened edge in a foil generating apparatus according to an embodiment of the present invention.

Fig. 3 is a schematic view of a partial structure of an anode plate with a thickened edge in a foil generating apparatus according to an embodiment of the present invention.

Fig. 4 is a schematic structural diagram of a liquid inlet and outlet unit in the green foil device provided by the embodiment of the invention.

Fig. 5 is a schematic diagram of an inclined surface of a secondary liquid inlet in the foil generating device according to the embodiment of the invention.

Fig. 6 is a schematic structural diagram of a regulating unit in the foil generating device according to the embodiment of the present invention.

Fig. 7 is a schematic partial structural diagram of a limiting mechanism of an adjusting unit in a foil generating device according to an embodiment of the present invention.

Fig. 8 is a schematic structural diagram of an adjustable unit in the foil generating apparatus according to an embodiment of the present invention.

Fig. 9 is a schematic structural diagram of a control unit in the foil generating device according to the embodiment of the present invention.

FIG. 10 is a schematic structural diagram of an adjustable unit and a control unit in a foil generating apparatus according to an embodiment of the present invention.

Fig. 11 is a flow chart of the intelligent control process for the copper foil thickness according to the present invention.

FIG. 12 is a flow chart of the process for controlling the lateral thickness of the copper foil according to the present invention.

Detailed Description

To facilitate understanding of those skilled in the art, the structure of the present invention will now be described in further detail by way of examples in conjunction with the accompanying drawings:

referring to fig. 1, a foil forming apparatus includes an anode unit 1 electrically connected to a positive electrode, a cathode roller 2 electrically connected to a negative electrode, a transfer unit 14 provided at one side of the cathode roller 2, a detection unit 15 for detecting a transverse thickness (i.e., a width direction) of a copper foil, and a secondary detection unit for detecting a longitudinal thickness of the copper foil; the anode unit 1 comprises an arc-shaped machine groove 3 and a plurality of anode plates 4 which are arranged at the upper end of the arc-shaped machine groove 3 in a radial sequence respectively; the foil generating device further comprises a liquid inlet and outlet unit for adjusting the volume and concentration of the solution in the arc-shaped machine groove 3, an adjusting unit for adjusting the distance between the cathode plate and the anode plate, an adjustable unit for intelligently controlling the transverse thickness of the copper foil and a regulating and controlling unit.

The number of the anode plates 4 is 10-30, and the number of the anode plates 4 is 18 in the embodiment.

As shown in figures 2-3, the device utilizes the heightening part to reduce the distance between the gap position of the adjacent anode plates and the cathode roller, thereby enabling the plating layer at the corresponding position to be thicker and effectively preventing the edge from being torn.

The anode plate 4 comprises a height increasing part 41 and an anode plate main body 42, the two side edges of the anode plate main body 42, which are arranged corresponding to the adjacent anode plate 4, are respectively provided with the corresponding height increasing part 41 in a connecting way, and the minimum distance between the height increasing part 41 and the cathode roller 2 is smaller than the distance between the anode plate main body 42 and the cathode roller 2; the maximum thickness of the raised part 41 is 0.1-10% of the thickness of the anode plate main body 42, and the width of the raised part 41 is 0.1-15% of the width of the anode plate 4.

The height of the raised portion 41 is too large, which may cause uneven coating and may cause the pitch of the anode plate body 42 to be unable to be finely adjusted. The height of the raised portion 41 is too small to effectively prevent edge tearing. Preferably, the maximum thickness of the raised portion 41 is 0.5 to 5% of the thickness of the anode plate main body 42, and the width of the raised portion 41 is 0.5 to 5% of the width of the anode plate 4. More preferably, the maximum thickness of the raised portion 41 is 1 to 3% of the thickness of the anode plate main body 42, and the width of the raised portion 41 is 1 to 3% of the width of the anode plate 4. In this embodiment, the two side edges of the anode plate main body 42 extend upward in an integrated streamline shape to gradually thicken to form the raised portion 41, the maximum thickness of the raised portion 41 is 2% of the thickness of the anode plate main body 42, and the width of the raised portion 41 is 2% of the width of the anode plate 4.

As shown in fig. 4, the solution inlet and outlet unit regulates and controls the uniformity of the concentration of the solution in the whole circular arc machine groove 3, so that the concentrations of the solutions on two sides of the circular arc machine groove 3 and the inlet liquid notch 8 tend to be close to each other, and the specific structure is as follows:

business turn over liquid unit contains to set up the axial feed liquor notch 8 of the radial central authorities of convex quick-witted groove 3, anode plate 4 sets up radially in proper order respectively to 3 both sides upper ends of convex quick-witted groove along the 8 left and right sides of feed liquor notch, clearance between negative pole roller 2 and all anode plates 4 forms the anode tank, convex quick-witted groove 3 in the both sides of feed liquor notch 8 all are provided with a plurality of intercommunications the second grade inlet 9 of anode tank, second grade inlet 9 is connected external corresponding solution tank through corresponding solution pump respectively with feed liquor notch 8, second grade inlet 9 is rectangular slit structure, and sets up position between the connecting gap of convex quick-witted groove 3 in adjacent a plurality of anode plates 4. In this embodiment, the splicing surface of the anode plate 4 is an inclined surface inclined upward.

The setting on inclined plane makes second grade inlet 9 upwards set up, avoids directly to cathode roll 2 feeding, plays the buffering effect, prevents that local production from burning the paper tinsel or the bubble problem. And a plurality of strip-shaped slit secondary liquid inlets 9 are additionally arranged to supplement additives, so that the concentration uniformity of the solution in the whole circular arc machine groove 3 is regulated, the concentration of the solution on two sides of the circular arc machine groove 4 is close to that of the liquid inlet notch 8, the thickness uniformity of the copper foil in the length direction is promoted to be improved, different additives such as brightening agents and the like can be added into the solution of the secondary liquid inlets 9 according to different stages, the rough surface crystal grains of the copper foil are fine, and the high-quality copper foil is produced.

As shown in fig. 5, a straight line AB formed by connecting a lower right end a of the anode plate 4 with a point B on the cathode roller 2 is defined to be tangent to the cathode roller 2, a straight line AC is defined by connecting the lower right end a of the anode plate 4 with an upper right end C of a second anode plate 4 adjacent to the upper end of the anode plate 4, an included angle between AC and AB is defined as α, an adjustment range of the inclined plane is defined as 2 α, and corresponding included angles α are respectively set to both sides with the tangent line AB as a center line (the adjustment range is associated with the thickness of the anode plate 4 and the distance between the anode plate 4 and the cathode roller), and an extension line of the straight line AD where the inclined plane is located falls within the adjustment range 2 α. Preferably, the straight line AD and the coincidence of straight line AB at inclined plane place, the inclination on this inclined plane can effectively avoid directly to the feeding of cathode roll 2, prolongs the distance between 9 exports of second grade inlet and the cathode roll 2 for liquid has sufficient buffer distance to avoid directly influencing cathode roll 2. If the inclination angle is too small, the local liquid concentration of the cathode roller 2 is rapidly increased, so that the thickness of the copper foil at the position is rapidly increased, and the overall electroplating effect is influenced; the inclination angle is crossed and is beaten the unable setting of one side, and on the other hand can produce certain vortex problem, all influences the quality of copper foil finally.

In other embodiments, the inlet slot 8 is also divided into a plurality of guide channels by corresponding partition plates, and each inlet guide channel is respectively connected with the solution pump through a corresponding metering valve and a multi-way pipe.

In other embodiments, the secondary inlet 9 is divided into a plurality of diversion channels by corresponding partition plates, each inlet diversion channel is connected to the solution pump through a corresponding metering valve and a multi-way pipe, the width of the diversion channel is 1-5 mm, the number of the diversion channels of the secondary inlet 9 is the same as that of the inlet notches 8 or is more than that of the inlet notches 8, preferably 15-25, and the number of the diversion channels of the secondary inlet 9 is the same as that of the inlet notches 8, and is 15. Divide into a plurality of water conservancy diversion passageways with second grade inlet 9 with the flow size of control, improve the horizontal homogeneity of copper foil, reduce the production of seersucker, soft wrinkle, utilize the accurate control feed liquor volume of metering valve, prevent that excessive feed liquor from leading to burning paper tinsel or uneven problem of thickness from producing.

In other embodiments, the aperture of the secondary liquid inlet 9 along the two sides of the circular arc machine groove 3 from the liquid inlet notch 8 is gradually increased, and the maximum aperture is smaller than the aperture of the liquid inlet notch 8, and the aperture of the secondary liquid inlet 9 is gradually increased more quickly to promote the concentration uniformity of each position as the solution concentration is lower the more the two sides of the circular arc machine groove 3 go up. The width of the liquid inlet notch 8 is defined as D, wherein the width of the topmost secondary liquid inlet 9 is 0.1-0.2D, the width is limited and is matched with a metering valve to control the liquid inlet flow of the solution, the local concentration is prevented from being excessively increased, and the foil burning risk and probability can be effectively reduced.

As a further step, a liquid outlet 10 is arranged at the upper end of the inner arc surface of the arc-shaped machine groove 3 and above the topmost anode plate 4, the liquid outlet 10 is communicated with a liquid drainage channel embedded in the arc-shaped machine groove 3, and an outlet of the liquid drainage channel is arranged on the outer side of the outer arc surface of the arc-shaped machine groove 3 and has a downward opening.

As shown in fig. 6 to 7, the adjusting unit can flexibly adjust the spacing between the cathode and the anode at each position to solve the problem of increasing the gap between the anode plate and the cathode roll, and can adjust the thickness in the length direction, and the specific structure is as follows: comprises a driving mechanism for driving the anode plate 4 to move and a limiting mechanism for limiting the anode plate 4 to move up and down.

As a further step, the driving mechanism comprises a plurality of screw rods 51 which respectively penetrate through and are screwed with the circular arc machine grooves 3, the positions of the circular arc machine grooves 3 corresponding to the anode plates 4 are provided with threaded holes which penetrate through the upper end and the lower end of the circular arc machine grooves 3, the screw rods 51 respectively penetrate through the circular arc machine grooves 3 through being in threaded connection with the corresponding threaded holes, and the tail ends of the screw rods are respectively in rotating connection with the back surfaces of the corresponding anode plates 4.

As a further step, the limiting mechanism comprises limiting plates 61 installed at the upper ends of the front side and the rear side of the circular arc-shaped machine groove 3, sliding blocks 63 fixedly connected to the two ends of the limiting plates are embedded into sliding grooves 62 formed in the limiting plates 61, the anode plate 4 is installed between the two limiting plates 61 in a vertically moving connection mode, and the sliding grooves 62 are formed in the positions, corresponding to the anode plate 4, of the inner side surfaces of the limiting plates 61. The distance between the cathode and the anode at each position can be flexibly adjusted to solve the problem that the gap between the anode plate 4 and the cathode roller 2 is enlarged, and the screw rod 51 is utilized to independently control each anode plate 4 to adjust the anode plates 4 in copper sulfate solutions with different concentrations in different ways, thereby improving the practicability.

Further, the part of the screw 51 connected with the back of the circular arc-shaped machine groove 3 is a non-threaded rod part, a part of the threaded hole communicated with the back of the circular arc-shaped machine groove 3 is provided with a non-threaded through hole, and the surface of the non-threaded through hole is provided with a corresponding sealing ring 7; specifically, the outer diameter of the sealing ring 7 is larger than the diameter of a through hole of the circular arc machine groove 3 for installing the screw rod, the sealing ring 7 is compressed during installation, and the sealing performance of the circular arc machine groove 3 is ensured, or an existing sealing mechanism is adopted.

In other embodiments, the anode unit 1 is provided with an anode thickening plate 18 with a thickness of 1-2 mm on the upper surface of the anode plate 4 between the liquid inlet slot opening 8 and the foil outlet end, the distance between the anode plate 4 and the cathode roller 2 is reduced by additionally arranging the anode thickening plate 18 on the rear side, the thickness of the copper foil in the length direction can be effectively adjusted, and along with the gradual generation of the copper foil, the thickness is increased after the particles are finer, and the quality of the copper foil can be ensured.

In other embodiments, the screw 51 includes a conductive portion connected to the anode plate 4 and an insulating portion disposed at one end of the arc-shaped slot 3, the conductive portions of the screw 51 are respectively connected to the corresponding first independent dc power supplies, and the input current is regulated by the respective first independent dc power supplies, and the insulating portion is sleeved with the corresponding insulating sleeve 16. The screw rod 51 is arranged into a conductive part and an insulating part, the insulating part is convenient for personnel to operate and adjust safely, the conductive part can directly guide current into the anode plate 4, a conductive layer is coated on the upper surface of the anode plate 4, and the current of each anode plate can be flexibly adjusted according to conditions so as to adjust the thickness of the copper foil.

In other embodiments, the driving mechanism 5 further includes a detachable plate 52 fixedly mounted on the back of the anode plate 4, the end of the screw 51 is rotatably connected to the back of the detachable plate 52, and the sliding block 63 is fixedly connected to two sides of the detachable plate 52, the detachable plate 52 is disposed to facilitate the anode plate 4 to be rotatably connected to the screw 51; and when the screw 51 is provided with a conductive portion, the detachable plate 52 is provided with a conductive material, ensuring smooth conduction of electric current to the anode plate 4.

As shown in fig. 8, the adjustable unit flexibly regulates and controls the current passing through each position of the anode plate 4 at the foil outlet end of the anode unit according to the thickness condition in the width direction to adjust the uniformity of the transverse thickness and realize the high-precision control of the thickness of the copper foil, so that the service cycle of the anode can be prolonged, and the adjustable unit has the following specific structure:

the anode plate 4 at the foil outlet end of the anode unit 1 is formed by splicing 10 to 30 short anode plates 11 along the width direction, preferably, the anode plate 4 at the foil outlet end of the anode unit 1 comprises 10 to 20 short anode plates 11, and in the embodiment, the anode plate 4 at the foil outlet end of the anode unit 1 preferably comprises 15 short anode plates 11; each short anode plate 11 is respectively connected with a corresponding second independent direct current power supply 17, the input current is regulated by the respective second independent direct current power supply 17, the anode of the second independent direct current power supply 17 is connected with the short anode plate 11, and the cathode of the second independent direct current power supply 17 is respectively connected with the cathode roller 2; the uniformity of the thickness cannot be accurately adjusted when the number of the short anode plates 11 is too small, and the cost is increased when the number is too large, and on the other hand, the dense parts are not beneficial to the installation of equipment; the position of the anode plate 4 of the arc-shaped machine groove 3 at the foil outlet end is provided with a corresponding secondary liquid inlet 9, the secondary liquid inlet 9 at the position is divided into a plurality of flow guide channels by corresponding division plates, each liquid inlet flow guide channel is respectively connected with the solution pump through a corresponding metering valve and a multi-way pipe, and the outlet of each flow guide channel is arranged in a clearance corresponding to the adjacent two short anode plates 11.

In other embodiments, a detection unit 15 for detecting the lateral thickness of the copper foil may be further included. Preferably, in order to improve the detection accuracy and precision, the detection units 15 are arranged at equal intervals in the transverse direction of the electrolytic copper foil, and the detection units 15 are arranged below the conveying unit 14 and the short anode plates 11 or between adjacent conveying rollers of the conveying unit 14.

In other embodiments, the short anode plates 11 are arranged at intervals, and two opposite side edges of the short anode plates 11 are extended upwards in an integrated streamline shape and are arranged in a gradually thickened manner, the distance between the gap position and the cathode roller is reduced through the thickened arrangement, and the thickness of the copper foil at the gap position and the non-gap position is further adjusted.

As shown in fig. 9, the adjusting and controlling unit can control the electrolysis area of the effective anode unit 1 at the corresponding position by flexibly controlling the rising and falling of the shielding plate 12 according to the thickness condition in the width direction, so as to adjust the thickness of the effective anode unit, realize high-precision control of the thickness of the copper foil, and prolong the service life of the anode plate 4. The concrete structure is as follows: contain and reciprocate to set up every the shield plate 12 of short strip anode plate 11 front end, shield plate 12 install in between negative pole roller 2 and the short strip anode plate 11, shield plate 12 reciprocates the setting through corresponding lift cylinder 13 individual drive respectively.

Further, the detection unit 15 and/or the lifting cylinder 13 and/or the second independent direct current power supply 17 and/or the metering valve are/is arranged in a linkage mode through a control system. The lifting and descending of each shielding plate 12 and/or the current of each short anode plate 11 are/is controlled in a linkage manner, so that the transverse thickness of the copper foil is adjusted, and the practicability and the control accuracy are improved.

As shown in fig. 10, an embodiment of the present invention further provides an intelligent control method for a copper foil thickness, which includes the following specific steps:

s1, introducing a copper sulfate electrolyte between the anode unit 1 and the cathode roller 2 to perform electrolytic foil generation, and generating an electrolytic copper foil on the surface of the cathode roller 2;

s2, the electrolytic copper foil is conveyed outwards through the conveying unit 14, the transverse thickness information of the electrolytic copper foil is detected through the detection unit in the conveying process, and the transverse thickness information is transmitted to the control system;

s3, the control system judges whether the transverse thickness information is in a preset range or not according to the transverse thickness information, if so, no operation is performed, and if not, the transverse coordinate of a position corresponding to the position, in which the transverse thickness information exceeds the preset range, in the electrolytic copper foil is obtained;

and S4, adjusting the thickness of the position corresponding to the position of the electrolytic copper foil with the transverse thickness information exceeding the preset range to be within the preset range.

In step S1, the copper sulfate electrolyte may be selected from existing copper sulfate electrolytes without limitation. In the electrolytic foil production process, control of specific parameters such as current density and concentration is also a conventional technique, and will not be described again here.

In step S2, the detecting units are disposed at equal intervals in the transverse direction of the electrolytic copper foil, and are sequentially numbered in the transverse direction, so that the thickness of the electrolytic copper foil in the transverse direction can be obtained in real time. The type of the detection unit is not limited, and a non-contact detection unit, such as an X-ray thickness gauge, may be selected.

In step S3, the preset range may be set according to a management and control requirement of an actual product. Specifically, for example, in the currently mainstream electrolytic copper foil of 4 to 8mm, the predetermined range may be within a tolerance of ± 20% of the actual thickness. For example, 5mm electrolytic copper foil, the predetermined range is 4.9mm to 5.1mm. And acquiring the transverse coordinate of the position corresponding to the transverse thickness information in the electrolytic copper foil exceeding the preset range according to the sequence label of the detection unit. Further, the transverse coordinate of the position corresponding to the transverse thickness information exceeding the preset range may be a single point or a plurality of points. When the transverse coordinates of the position corresponding to the transverse thickness information exceeding the preset range comprise a plurality of continuous points (and cannot be eliminated through subsequent adjustment), the transverse coordinates (with the thickness as the vertical coordinate) can be fitted to form a changing curve, so that the coordinates of the highest point and/or the lowest point are obtained. And when the thickness corresponding to the highest point/lowest point coordinate cannot be eliminated through adjustment subsequently, defining the highest point/lowest point coordinate as a damaged position, and further sending corresponding maintenance personnel to perform quick positioning and maintenance.

In step S4, in other embodiments, the method may further include:

s41, adjusting the thickness of the position corresponding to the transverse thickness information exceeding the preset range in the electrolytic copper foil by controlling the lifting and the falling of the shielding plate 12 at the position corresponding to the position exceeding the preset range so as to enable the thickness to be within the preset range.

In step S41, the height of the shielding plate 12 at the position corresponding to the position exceeding the preset range is controlled, so that the electrolysis area of the effective anode unit 1 at the corresponding position can be controlled to adjust the thickness thereof. Specifically, if the thickness of the copper foil at the corresponding position is thick, the shielding plate 12 at the corresponding position can be lowered to partially shield the copper foil so as to reduce the generation of the copper foil at the corresponding position; if the copper foil thickness of a few positions is thinner, the shielding of the shielding plate 12 to the anode unit 1 is reduced to increase the generation of the copper foil at the position, and the effect of energy saving can be achieved by combining intelligent control.

In step S4, in other embodiments, the method may further include:

and S42, adjusting the thickness of the position corresponding to the transverse thickness information exceeding the preset range in the electrolytic copper foil by controlling the current of the short anode plate 11 exceeding the corresponding position of the preset range so as to enable the transverse thickness information to be in the preset range.

In step S42, the current of the short anode plates 11 at the corresponding positions exceeding the preset range is controlled, so that the electrolysis efficiency at the corresponding positions can be controlled to adjust the thickness of the short anode plates. Specifically, if the copper foil at the corresponding position is thick, the current of the short anode plate 11 at the position can be reduced to reduce the generation of the copper foil at the position; if the thickness of the copper foil at a few positions is small, the current of the short anode plate 11 at the position is increased to increase the generation of the copper foil at the position.

In step S42, in other embodiments, the method may further include:

s421, obtaining the current regulating quantity needed by the thickness regulation exceeding the preset range and setting the current preset range;

s422, the control system judges whether the current regulation is in a current presetting range according to the transverse thickness information, if so, the thickness is regulated by controlling the current of the short anode plates 11 at the corresponding positions, so that the transverse thickness information is in a preset range; if not, when the current regulation reaches the end value of the current pre-regulation range, keeping the end value unchanged, and simultaneously entering step S423; specifically, the current preset range may be set according to a control requirement of an actually produced product, a maximum value of the current preset range is set to 80-95% of an adjustable maximum limit value of current when the transverse thickness information is obtained, and a minimum value of the current preset range is set to 105-120% of an adjustable minimum limit value of current when the transverse thickness information is obtained.

And S423, adjusting the thickness of the position corresponding to the position of the transverse thickness information in the electrolytic copper foil exceeding the preset range by controlling the copper sulfate electrolyte flow of the secondary liquid inlet 9 exceeding the position corresponding to the current preset range, so that the thickness is adjusted within the preset range under the condition of reducing energy consumption.

In step S4, in other embodiments, the method may further include:

s43, the thickness of the position corresponding to the position of the transverse thickness information in the electrolytic copper foil exceeding the preset range is adjusted to be within the preset range by controlling the flow of the copper sulfate electrolyte of the secondary liquid inlet 9 exceeding the position corresponding to the preset range.

In step S43, the copper sulfate electrolyte flow rate of the secondary liquid inlet 9 exceeding the corresponding position of the preset range is controlled, so as to control the copper sulfate electrolyte concentration at the corresponding position and adjust the thickness of the copper sulfate electrolyte. Specifically, if the copper foil at the corresponding position is thicker, the concentration of the copper sulfate electrolyte at the position can be weakened to reduce the generation of the copper foil at the position; if the thickness of the copper foil at a few positions is small, the concentration of the copper sulfate electrolyte at the position is increased.

In step S4, in another embodiment, the steps S41, S42, and S43 may be controlled in a linkage manner, so as to quickly adjust the thickness of the corresponding position. Specifically, when the transverse coordinate of the position corresponding to the transverse thickness information exceeding the preset range includes a plurality of continuous points, or when the thickness cannot be adjusted within the preset range by independently controlling the S41, S42 and S43, the lifting and lowering of the shielding plate 12, the current of the short anode plate 11 and the copper sulfate electrolyte flow of the secondary liquid inlet 9 can be controlled in a linked manner to perform rapid control.

In step S4, in other embodiments, the method may further include:

the liquid inlet notch 8 is also divided into a plurality of flow guide channels by corresponding partition plates, and each liquid inlet flow guide channel is connected with the solution pump through a corresponding metering valve and a multi-way pipe. The liquid inlet amount is controlled by controlling the metering valves of the flow guide channels, and the liquid inlet amount and the steps S41, S42 and S43 can be controlled in a linkage manner, so that the thickness adjustment of the corresponding position is quickly realized.

After step S4, the method may further include:

and S5, acquiring corresponding control parameters of each type of electrolytic copper foil in the production process. Therefore, in the process of generating the electrolytic copper foil with the type, the control parameters can be quickly called for production, so that the dependence on manpower can be greatly reduced, and automatic control is realized.

The foregoing 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 decorations can be made without departing from the principle of the present invention, and these modifications and decorations should also be regarded as the protection scope of the present invention.

Claims (7)

1. The utility model provides a give birth to paper tinsel device with many additives add mouth, includes the positive pole unit (1) of being connected with the positive electricity, cathode roll (2) of being connected with the negative electricity, positive pole unit (1) contains convex quick-witted groove (3), the radial central authorities axial in convex quick-witted groove (3) is provided with feed liquor notch (8), radially is provided with polylith anode plate (4) respectively along feed liquor notch (8) left and right sides to convex quick-witted groove (3) both sides upper end in proper order, the clearance that sets up between cathode roll (2) and all anode plate (4) forms anode tank, its characterized in that: convex quick-witted groove (3) in the both sides of feed liquor notch (8) all be provided with a plurality of intercommunications second grade inlet (9) in anode tank, second grade inlet (9) are rectangular slit structure, second grade inlet (9) and feed liquor notch (8) are respectively through corresponding solution pump connection external corresponding solution tank.

2. A green foil apparatus having multiple additive addition ports as recited in claim 1, wherein: the splicing surface of the anode plate (4) is an inclined surface which inclines upwards.

3. A green foil apparatus having multiple additive addition ports as recited in claim 1, wherein: the secondary liquid inlet (9) is arranged at the position of the circular arc machine groove (3) between the connecting gaps of the adjacent anode plates (4).

4. A green foil apparatus having multiple additive addition ports as recited in claim 1, wherein: the secondary liquid inlet (9) is divided into a plurality of flow guide channels by corresponding partition plates, and each liquid inlet flow guide channel is connected with the solution pump through a corresponding metering valve and a multi-way pipe.

5. The green foil assembly of claim 4, wherein: the width of the flow guide channel is 0.1-5 mm.

6. A green foil apparatus having multiple additive addition ports as recited in claim 1, wherein: the caliber of the secondary liquid inlet (9) at two sides of the arc-shaped machine groove (3) is gradually increased along the liquid inlet groove opening (8), and the maximum caliber is smaller than that of the liquid inlet groove opening (8).

7. A green foil apparatus having multiple additive addition ports as recited in claim 1, wherein: the upper end position of the inner arc surface of the arc-shaped machine groove (3) and the upper side of the topmost anode plate (4) are provided with a liquid outlet (10), the liquid outlet (10) is communicated with a liquid drainage channel embedded in the arc-shaped machine groove (3), and the outlet of the liquid drainage channel is arranged on the outer arc surface outer side of the arc-shaped machine groove (3) and is downward in opening.

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