CN110872724A - Method and device for preparing electroplating liquid medicine - Google Patents
Method and device for preparing electroplating liquid medicine Download PDFInfo
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- CN110872724A CN110872724A CN201811018337.XA CN201811018337A CN110872724A CN 110872724 A CN110872724 A CN 110872724A CN 201811018337 A CN201811018337 A CN 201811018337A CN 110872724 A CN110872724 A CN 110872724A
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/12—Process control or regulation
- C25D21/14—Controlled addition of electrolyte components
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/04—Electroplating: Baths therefor from solutions of chromium
- C25D3/06—Electroplating: Baths therefor from solutions of chromium from solutions of trivalent chromium
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/12—Electroplating: Baths therefor from solutions of nickel or cobalt
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/38—Electroplating: Baths therefor from solutions of copper
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Abstract
The application discloses a method and a device for blending electroplating liquid medicine, aiming at improving the stability of blending electroplating liquid medicine and simplifying the blending process. One method comprises the following steps: obtaining the current content of each component in the electroplating liquid medicine; grouping the components; comparing the current content of each component in each group with a standard data range; and outputting each group of allocation schemes according to the result of the larger value and the smaller value. The other method comprises the following steps: the mobile terminal selects an electroplating liquid medicine page needing to be prepared through a two-dimensional code generated by a WeChat scanning WeChat small program, obtains the current content of each component in the electroplating liquid medicine, transmits the current content of each component in the electroplating liquid medicine to a calculator, so that the current content of each component in the electroplating liquid medicine is compared with a standard data range respectively, and a preparation scheme is output according to the result of the comparison.
Description
Technical Field
The invention relates to the technical field of gravure plate making, in particular to a method and a device for preparing electroplating liquid medicine.
Background
In gravure plate-making industry, electroplating process occupies a very important position, the stability of electroplating liquid medicine directly influences the quality of products, the cost of electroplating consumables occupies 20% -30% of enterprise operating cost, but the technical scheme for allocating electroplating liquid medicine provided by the prior art is low in stability and complex in process, and the production efficiency is greatly reduced.
Therefore, how to improve the stability of the electroplating solution and simplify the preparation process becomes an important issue to be studied by those skilled in the art.
Disclosure of Invention
In view of the above, the present invention provides a method and a device for dispensing electroplating solution to solve the above technical problems. The specific scheme is as follows:
a method for preparing electroplating liquid medicine is applied to gravure plate-making industry and comprises the following steps:
obtaining the current content of each component in the electroplating liquid medicine;
grouping the components;
comparing the current content of each component in each group with a standard data range;
and outputting each group of allocation schemes according to the result of the larger value and the smaller value.
Optionally, the obtaining of the current content of each component in the electroplating liquid medicine includes obtaining the current content of each component of the electroplating hard chromium liquid medicine, and each component of the electroplating hard chromium liquid medicine includes chromic anhydride, sulfuric acid, trivalent chromium and chloride ions;
said grouping said components comprises grouping said components into three groups, said chromic anhydride and sulfuric acid being a first group, said trivalent chromium being a second group, said chloride ions being a third group;
said comparing the current content of said ingredients within each group to a standard data range respectively comprises comparing chromic anhydride and sulfuric acid in said first group to chromic anhydride and sulfuric acid in said standard data range respectively, comparing trivalent chromium in said second group to trivalent chromium in said standard data range, and comparing chloride ions in said third group to chloride ions in said standard data range;
and outputting each group of allocation schemes according to the result of the larger value, wherein the outputting comprises outputting a first group of allocation schemes, outputting a second group of allocation schemes and outputting a third group of allocation schemes.
Optionally, the obtaining of the current content of each component in the electroplating liquid medicine includes obtaining the current content of each component of the alkali copper liquid medicine, and each component of the alkali copper liquid medicine includes copper ions and a pH value;
the grouping of the components comprises dividing the components into two groups, wherein the copper ions are in a fourth group, and the pH value is in a fifth group;
comparing the current content of each component in each group with a standard data range, respectively, comprising comparing copper ions in the fourth group with copper ions in the standard data range, and comparing pH values in the fifth group with pH values in the standard data range;
and outputting each group of blending schemes according to the result of the larger value and the smaller value, wherein the step of outputting the fourth group of blending schemes and the step of outputting the fifth group of blending schemes are included.
Optionally, the obtaining of the current content of each component in the electroplating liquid medicine includes obtaining the current content of each component of the nickel liquid medicine, and each component of the nickel liquid medicine includes nickel sulfate, nickel chloride and boric acid;
the grouping of the components comprises grouping the components into three groups, wherein the nickel sulfate is a sixth group, the nickel chloride is a seventh group, and the boric acid is an eighth group;
said comparing the current content of said ingredients within each grouping to a standard data range respectively comprises comparing nickel sulfate in said sixth group to nickel sulfate in said standard data range, comparing nickel chloride in said seventh group to nickel chloride in said standard data range, comparing boric acid in said eighth group to boric acid in said standard data range;
and outputting each group of allocation schemes according to the result of the larger value, wherein the step of outputting each group of allocation schemes comprises outputting a sixth group of allocation schemes, outputting a seventh group of allocation schemes and outputting an eighth group of allocation schemes.
Optionally, the obtaining of the current content of each component in the electroplating liquid medicine comprises obtaining the current content of each component of the acid copper liquid medicine, wherein each component of the acid copper liquid medicine comprises copper sulfate, sulfuric acid and chloride ions;
the grouping of the components comprises grouping the components into three groups, wherein the copper sulfate is a ninth group, the sulfuric acid is a tenth group, and the chloride ions are the tenth group;
said comparing the current content of said ingredients within each group to a standard data range respectively comprises comparing copper sulfate in said ninth group to copper sulfate in said standard data range, comparing sulfuric acid in said tenth group to sulfuric acid in said standard data range, comparing chloride ions in said tenth group to chloride ions in said standard data range;
and outputting each group of blending schemes according to the result of the larger value, wherein the step of outputting each group of blending schemes comprises outputting a ninth group of blending schemes, outputting a tenth group of blending schemes and outputting an eleventh group of blending schemes.
The utility model provides a device of allotment electroplating solution, is applied to in the gravure plate-making trade, includes:
the acquisition module is used for acquiring the current content of each component in the electroplating liquid medicine;
the grouping module is used for grouping the components;
the comparison module is used for comparing the current content of each component in each group with a standard data range;
and the output module is used for outputting the allocation scheme of each group according to the result of the larger value and the smaller value.
Optionally, the obtaining module includes a first obtaining unit, where the first obtaining unit is configured to obtain current contents of each component of the hard chromium electroplating chemical, and each component of the hard chromium electroplating chemical includes chromic anhydride, sulfuric acid, trivalent chromium, and chloride ions;
the grouping module comprises a first grouping unit for grouping the components into three groups, the chromic anhydride and sulfuric acid being a first group, the trivalent chromium being a second group, and the chloride ions being a third group;
the comparison module comprises a first comparison unit for comparing chromic anhydride and sulfuric acid in the first set with chromic anhydride and sulfuric acid in the standard data range, respectively, trivalent chromium in the second set with trivalent chromium in the standard data range, and chloride ions in the third set with chloride ions in the standard data range;
the output module comprises a first output unit, and the first output unit is used for outputting a first group of blending schemes, outputting a second group of blending schemes and outputting a third group of blending schemes.
Optionally, the obtaining module includes a second obtaining unit, where the second obtaining unit is configured to obtain current contents of components of the alkali copper liquid medicine, and the components of the alkali copper liquid medicine include copper ions and a pH value;
the grouping module comprises a second grouping unit, the second grouping unit is used for dividing the components into two groups, the copper ions are in a fourth group, and the pH value is in a fifth group;
the comparison module comprises a second comparison unit for comparing the copper ions in the fourth group with the copper ions in the standard data range, and for comparing the pH values in the fifth group with the pH values in the standard data range;
the output module comprises a second output unit, and the second output unit is used for outputting the fourth group of blending schemes and outputting the fifth group of blending schemes.
Optionally, the obtaining module includes a third obtaining unit, where the third obtaining unit is configured to obtain current contents of components of the nickel liquid medicine, and the components of the nickel liquid medicine include nickel sulfate, nickel chloride, and boric acid;
the grouping module comprises a third grouping unit, wherein the third grouping unit is used for grouping the components into three groups, the nickel sulfate is a sixth group, the nickel chloride is a seventh group, and the boric acid is an eighth group;
the comparison module comprises a third comparison unit for comparing the nickel sulfate in the sixth group with the nickel sulfate in the standard data range, the nickel chloride in the seventh group with the nickel chloride in the standard data range, the boric acid in the eighth group with the boric acid in the standard data range;
the output module comprises a third output unit, and the third output unit is used for outputting a sixth group of blending schemes, outputting a seventh group of blending schemes and outputting an eighth group of blending schemes.
Optionally, the obtaining module includes a fourth obtaining unit, where the fourth obtaining unit is configured to obtain current contents of components of the acid copper chemical, where the components of the acid copper chemical include copper sulfate, sulfuric acid, and chloride ions;
the grouping module comprises a fourth grouping unit for grouping the components into three groups, the copper sulfate is a ninth group, the sulfuric acid is a tenth group, and the chloride ions are the tenth group;
the comparison module comprises a fourth comparison unit for comparing copper sulfate in the ninth group with copper sulfate in the standard data range, sulfuric acid in the tenth group with sulfuric acid in the standard data range, and chloride ions in the tenth group with chloride ions in the standard data range;
the output module comprises a fourth output unit, and the fourth output unit is used for outputting a ninth group of blending schemes, outputting a tenth group of blending schemes and outputting an eleventh group of blending schemes.
Compared with the prior art, the invention has the following beneficial effects:
the method and the device for preparing the electroplating liquid medicine have the advantages of simple preparation steps, high stability of the electroplating liquid medicine, no electroplating liquid medicine loss problem caused by wrong preparation and improvement of production efficiency.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.
FIG. 1 is a flow chart of a method for dispensing an electroplating solution according to an embodiment of the present invention.
FIG. 2 is a flow chart of another method for dispensing electroplating solution according to an embodiment of the present invention.
FIG. 3 is a schematic diagram of an apparatus for dispensing electroplating solution according to an embodiment of the present invention.
FIG. 4 is a flow chart of another method for dispensing electroplating solution according to an embodiment of the present invention.
FIG. 5 is a schematic diagram of a system for dispensing electroplating solution according to an embodiment of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1 and fig. 2, the present embodiment provides a method for preparing an electroplating solution, which is applied to the gravure printing industry, and specifically includes the following steps:
step S1: and obtaining the current content of each component in the electroplating liquid medicine.
Step S2: and grouping the components.
Step S3: comparing the current content of each component in each group with a standard data range.
Step S4: and outputting each group of allocation schemes according to the result of the larger value and the smaller value.
Further, the step S1 includes a step S5, specifically, obtaining current contents of each component of the hard chromium electroplating chemical, where each component of the hard chromium electroplating chemical includes chromic anhydride, sulfuric acid, trivalent chromium and chloride ions;
the step S2 includes a step S6, specifically, the components are divided into three groups, the chromic anhydride and sulfuric acid are a first group, the trivalent chromium is a second group, and the chloride ion is a third group;
the step S3 includes a step S7 of comparing the chromic anhydride and the sulfuric acid in the first group with the chromic anhydride and the sulfuric acid in the standard data range, respectively, comparing the trivalent chromium in the second group with the trivalent chromium in the standard data range, and comparing the chloride ions in the third group with the chloride ions in the standard data range;
the step S4 includes a step S8, which is to output a first group of blending schemes, output a second group of blending schemes, and output a third group of blending schemes.
Further, in the embodiment, the standard data range of chromic anhydride is 230-280 g/L, the standard data range of sulfuric acid is 2.5-3.3 g/L, the standard data range of trivalent chromium is 2.0-5.0 g/L, and the standard data range of chloride ion is less than 200 ppm.
The current content of chromic anhydride is H1g/L, the current content of the sulfuric acid is H2g/L, acid ratio between chromic anhydride and sulfuric acid equal to H3The current content of the trivalent chromium is H4g/L, the current content of the chloride ion is H5ppm, where g/L and ppm are units.
Thus, the first set of formulation protocols is embodied as the following procedure.
When inputting value H1＜230，H2When the content of the organic acid is less than 2.5,
the first set of blending recipes is output as: the content of the components of the plating solution is low, and chromic anhydride is required to be supplemented into the bath.
When inputting value H1＜230，H2∈[2.5-3.3]When the temperature of the water is higher than the set temperature,
the first set of blending recipes is output as: when the component content of the plating solution is abnormal, chromic anhydride is required to be supplemented into the tank.
When inputting value H1＜230，H2>At the time of 3.3, the temperature of the molten steel is higher,
the first set of blending recipes is output as: when the content of the components of the plating solution is abnormal, the plating solution needs to be extracted to reduce the volume of the plating solution, then barium carbonate is added, and chromic anhydride is added.
When inputting value H1∈[230,280]，H2<At the time of 2.5, the temperature of the mixture,
the first set of blending recipes is output as: the acid ratio of the plating solution is too low, and sulfuric acid needs to be added for adjustment.
When inputting value H1∈[230,280]，H2∈[2.5-3.3]Then, judge H3If H is3<1.1，
The first set of blending recipes is output as: the acid ratio of the plating solution is too low, and sulfuric acid needs to be added for adjustment.
When inputting value H1∈[230,280]，H2∈[2.5-3.3]Then, judge H3If H is3∈[1.1,1.2]，
The first set of blending recipes is output as: the plating solution content is normal.
When inputting value H1∈[230,280]，H2∈[2.5-3.3]Then, judge H3，H3>When the pressure of the mixture is 1.2 times,
the first set of blending recipes is output as: when the acid ratio of the plating solution is too high, chromic anhydride is added for adjustment.
When inputting value H1∈[230,280]，H2>And 3.3, outputting a first group of blending schemes as follows: when the content of the components of the plating solution is abnormal, the plating solution needs to be extracted to reduce the volume of the plating solution, and then barium carbonate is added;
when inputting value H1＞280，H2When the output value is less than or equal to 3.3, outputting a first group of blending schemes as follows: when the plating solution has abnormal component content, sulfuric acid is added, and the Baume degree is diluted to 21.
The second group of formulation schemes is embodied as the following procedure.
When inputting value H4<And 2, outputting a second group of blending schemes as follows: the content of trivalent chromium is low, and alcohol is recommended to be added.
When inputting value H4∈[2,5]And then outputting a second group of blending schemes as follows: the content of trivalent chromium is normal.
When inputting value H4>And 5, outputting a second group of blending schemes as follows: the trivalent chromium content is higher, and the platelet is recommended to be used for electrolysis under the conditions of 60 ℃ and 60A/dm ^ 2.
The third set of formulation is specifically the following procedure.
When inputting value H5Less than or equal to 200, and outputting a third group of blending schemes as follows: the lower chloride ion content suggests continuing to maintain the bath composition stable.
When inputting the value 200<H5And outputting a third group of blending schemes as follows: please keep the temperature twice a week, and perform electrolysis at 60 ℃ under the electrolysis treatment of 60A/dm ^ 2.
Further, the step S1 further includes obtaining current contents of each component of the alkali copper chemical, where each component of the alkali copper chemical includes copper ions and a pH value.
Specifically, the grouping of the components comprises grouping the components into two groups, the copper ions are in a fourth group, and the pH value is in a fifth group.
Comparing the current content of each component in each group to a standard data range, respectively, comprises comparing copper ions in the fourth group to copper ions in the standard data range, and comparing pH values in the fifth group to pH values in the standard data range.
And outputting each group of blending schemes according to the result of the larger value and the smaller value, wherein the step of outputting the fourth group of blending schemes and the step of outputting the fifth group of blending schemes are included.
Specifically, the present content of copper ions is K1g/L. In the standard data range, the standard data range of the copper ions is 5.0-10.0 g/L, and the standard data range of the pH value is 9.2-10.0.
Therefore, when K1When the number is less than 5, the fourth adjustment scheme is as follows: and supplementing DY-Cu and DY-Cu-E, supplementing DY-Cu-pHA, and adjusting the pH value to the standard data range.
The reason for the reduction of the copper ion content can be found from the following aspects:
(1) checking whether liquid leaks or water is supplemented until the liquid level is high;
(2) the supplement agent DY-Cu-E is abnormally supplemented, the content of the E agent in a copper groove is low, so that the copper dissolution of copper balls is abnormal, and the supplement agent is recommended to be supplemented according to 2500 mL/KAH;
(3) checking whether the copper ball is passivated, and suggesting that 5 percent of hydrogen peroxide and 5 percent of dilute sulfuric acid are used for soaking in sequence;
(4) less copper balls and small anode copper area, and the area ratio of the cathode to the anode is suggested to be 1: 1.5.
when K is1And when the number is more than 10, the fourth group of adjustment schemes is as follows: and analyzing the reason of the rise of the copper ions.
Among them, the reasons for the rise of copper ions are as follows:
(1) and checking whether the liquid level is low or not, and forgetting to replenish water.
(2) Too many copper balls, the anode copper area is big, the area ratio of the copper balls taken out to the cathode and the anode is suggested to be 1: 1.5.
when the pH is less than 9.2, the fifth set of adjustments is: and supplementing DY-Cu-pHA to adjust the pH value to 9.5.
When the pH value is more than 10.0, the fifth group of adjustment schemes is as follows: the pH was adjusted to 9.5 by addition of 10% dilute sulfuric acid.
Further, the step S1 further includes obtaining current contents of each component of the nickel liquid medicine, where each component of the nickel liquid medicine includes nickel sulfate, nickel chloride, and boric acid.
The grouping of the components comprises grouping the components into three groups, wherein the nickel sulfate is a sixth group, the nickel chloride is a seventh group, and the boric acid is an eighth group.
The comparing the current content of the ingredients in each group to a standard data range includes comparing the nickel sulfate in the sixth group to the nickel sulfate in the standard data range, comparing the nickel chloride in the seventh group to the nickel chloride in the standard data range, and comparing the boric acid in the eighth group to the boric acid in the standard data range.
And outputting each group of allocation schemes according to the result of the larger value, wherein the step of outputting each group of allocation schemes comprises outputting a sixth group of allocation schemes, outputting a seventh group of allocation schemes and outputting an eighth group of allocation schemes.
Specifically, the current contents of nickel sulfate, nickel chloride and boric acid are respectively marked as B1、B3、B3g/L。
The standard data range of the nickel sulfate is 200-250g/L, the standard data range of the nickel chloride is 35-45g/L, and the standard data range of the boric acid is 40-45 g/L.
Therefore, when B1When the number is less than 200, the sixth group of adjustment schemes is as follows: and supplementing nickel sulfate.
When B is present1Above 250, the sixth set of adjustments is: the nickel sulfate is adjusted to 200-250g/L by adding water for dilution.
When B is present1∈[200，250]Then, the sixth group of adjustment schemes is: the content of nickel sulfate is normal.
When B is present2When less than 35, the seventh set of adjustment schemes is: replenishing nickel chloride.
When B is present2Above 45, the seventh set of adjustments is: adding water to dilute the solution to adjust the nickel chloride to 35-45 g/L.
When B is present2∈[35,45]Then, the seventh group of adjustment schemes is: the content of nickel chloride is normal.
When B is present3When less than 40, the eighth group of adjustment schemes is: and adding boric acid.
When B is present3And when the number is more than 45, the eighth group of adjustment schemes comprises: adding water to dilute the mixture to adjust the boric acid to 40-45 g/L.
When B is present3∈[40,45]Then, the eighth group of adjustment schemes is: the boric acid content is normal.
Further, the step S1 includes obtaining current contents of each component of the acid copper chemical, where each component of the acid copper chemical includes copper sulfate, sulfuric acid, and chloride ions.
The grouping of the components comprises grouping the components into three groups, wherein the copper sulfate is a ninth group, the sulfuric acid is a tenth group, and the chloride ions are the tenth group.
The comparing the current content of the ingredients in each group to a standard data range separately comprises comparing copper sulfate in the ninth group to copper sulfate in the standard data range, comparing sulfuric acid in the tenth group to sulfuric acid in the standard data range, and comparing chloride ions in the tenth group to chloride ions in the standard data range.
And outputting each group of blending schemes according to the result of the larger value, wherein the step of outputting each group of blending schemes comprises outputting a ninth group of blending schemes, outputting a tenth group of blending schemes and outputting an eleventh group of blending schemes.
Specifically, the current contents of copper sulfate, sulfuric acid and chloride ion are respectively marked as E1、E2、E3g/L。
The standard data ranges of the copper sulfate, the sulfuric acid and the chloride ions are 190-220g/L, 60-70g/L and 80-150 ppm respectively.
Therefore, when E1When the adjustment rate is less than 190, the ninth group of adjustment schemes is as follows: and supplementing copper sulfate.
When E is1Above 220, the ninth set of adjustment schemes is: adding water to dilute the solution to adjust the copper sulfate to 190-220 g/L.
When E is1∈[200,250]Then, the ninth group of adjustment schemes is: the copper sulfate content is normal.
When E is2When less than 60, the tenth set of adjustment schemes is: supplementing sulfuric acid.
When E is2Above 70, the tenth set of adjustments is: adding water to dilute the mixture to adjust the sulfuric acid to 60-70 g/L.
When E is2∈[60,70]Then, the tenth group of adjustment schemes is: the sulfuric acid content is normal.
When E is3When less than 80, the eleventh set of adjustments is: hydrochloric acid is supplemented.
When E is3Above 80, the eleventh set of adjustments is: the hydrochloric acid content is normal.
In conclusion, the method for preparing the electroplating solution provided by the embodiment has the advantages of simple preparation steps, high stability of the electroplating solution, no problem of electroplating solution loss caused by a wrong preparation, and improvement of production efficiency.
Referring to fig. 3, in an alternative embodiment of the present application, an apparatus for dispensing an electroplating solution is provided, which is applied to the gravure printing industry, and includes:
an obtaining module S101, configured to obtain current contents of components in the electroplating liquid medicine;
a grouping module S102, configured to group the components;
a comparison module S103, configured to compare the current content of each component in each group with a standard data range respectively;
and the output module S104 is used for outputting the allocation scheme of each group according to the result of the larger value and the smaller value.
Further, the obtaining module S101 includes a first obtaining unit, where the first obtaining unit is configured to obtain current contents of each component of the hard chromium electroplating solution, where each component of the hard chromium electroplating solution includes chromic anhydride, sulfuric acid, trivalent chromium, and chloride ions. The grouping module S102 includes a first grouping unit for grouping the components into three groups, the chromic anhydride and sulfuric acid being the first group, the trivalent chromium being the second group, and the chloride ion being the third group. The comparing module S103 comprises a first comparing unit for comparing the chromic anhydride and the sulfuric acid in the first group with the chromic anhydride and the sulfuric acid in the standard data range, respectively, the trivalent chromium in the second group with the trivalent chromium in the standard data range, and the chloride ions in the third group with the chloride ions in the standard data range. The output module S104 includes a first output unit, and the first output unit is configured to output a first group of blending schemes, output a second group of blending schemes, and output a third group of blending schemes.
Further, the obtaining module S101 includes a second obtaining unit, where the second obtaining unit is configured to obtain current contents of components of the alkali-copper liquid medicine, where the components of the alkali-copper liquid medicine include copper ions and a pH value; the grouping module S102 includes a second grouping unit for grouping the components into two groups, the copper ions being in a fourth group, and the pH being in a fifth group. The comparing module S103 comprises a second comparing unit for comparing the copper ions in the fourth group with the copper ions in the standard data range, and for comparing the pH value in the fifth group with the pH value in the standard data range. The output module S104 includes a second output unit, and the second output unit is configured to output a fourth group of blending schemes and a fifth group of blending schemes.
Further, the obtaining module S101 includes a third obtaining unit, where the third obtaining unit is configured to obtain current contents of components of the nickel liquid medicine, and the components of the nickel liquid medicine include nickel sulfate, nickel chloride, and boric acid. The grouping module S102 includes a third grouping unit, which is configured to group the components into three groups, where the nickel sulfate is a sixth group, the nickel chloride is a seventh group, and the boric acid is an eighth group. The comparing module S103 includes a third comparing unit for comparing the nickel sulfate in the sixth group with the nickel sulfate in the standard data range, comparing the nickel chloride in the seventh group with the nickel chloride in the standard data range, and comparing the boric acid in the eighth group with the boric acid in the standard data range. The output module S104 includes a third output unit, and the third output unit is configured to output a sixth group of blending schemes, a seventh group of blending schemes, and an eighth group of blending schemes.
Further, the obtaining module S101 includes a fourth obtaining unit, where the fourth obtaining unit is configured to obtain current contents of each component of the acid copper chemical, where each component of the acid copper chemical includes copper sulfate, sulfuric acid, and chloride ions. The grouping module S102 includes a fourth grouping unit for grouping the components into three groups, the copper sulfate is a ninth group, the sulfuric acid is a tenth group, and the chloride ions are the tenth group. The comparison module S103 comprises a fourth comparison unit for comparing copper sulfate in the ninth group with copper sulfate in the standard data range, comparing sulfuric acid in the tenth group with sulfuric acid in the standard data range, and comparing chloride ions in the tenth group with chloride ions in the standard data range. The output module S104 includes a fourth output unit, and the fourth output unit is configured to output a ninth group of blending schemes, a tenth group of blending schemes, and an eleventh group of blending schemes.
The apparatus for dispensing electroplating solution provided in this embodiment can implement the method for dispensing electroplating solution, and the specific working method thereof has been described in the above method, and is not described herein again.
Still further, in another embodiment of the present application, there is provided a computing device comprising:
a memory for storing a program;
and the processor is used for realizing the steps of the method for preparing the electroplating liquid medicine when the program is executed.
Still further, in another embodiment of the present application, a computer-readable storage medium is provided, which stores a program, and the program is executed by a processor to implement the steps of the method for dispensing electroplating solution.
Referring to fig. 4, optionally, in another embodiment of the present application, another method for dispensing an electroplating solution is further provided, including:
step S9: the mobile terminal scans the two-dimensional code generated by the WeChat applet through the WeChat so as to log in the WeChat applet, wherein the WeChat user ID identification information is stored in the server.
Step S10: selecting the electroplating solution page to be prepared.
Step S11: and acquiring the current content of each component in the electroplating liquid medicine, transmitting the current content of each component in the electroplating liquid medicine to a calculator so that the current content of each component in the electroplating liquid medicine is compared with a standard data range, outputting a blending scheme according to the result of the comparison and transmitting the blending scheme to the server.
Further, the current content of each component in the electroplating liquid medicine is obtained, and the current content of each component in the electroplating liquid medicine is transmitted to a calculator, wherein the current content of each component in the electroplating hard chromium liquid medicine, the current content of each component in the alkali copper liquid medicine, the current content of each component in the nickel liquid medicine and the current content of each component in the acid copper liquid medicine are obtained.
The step of comparing the current content of each component in the electroplating liquid medicine with a standard data range respectively comprises the step of comparing the current content of each component in the electroplating hard chromium liquid medicine, the current content of each component in the alkali copper liquid medicine, the current content of each component in the nickel liquid medicine and the current content of each component in the acid copper liquid medicine with data in the standard data range respectively.
And outputting a blending scheme according to the result of the larger size and transmitting the blending scheme to the server, wherein the step of outputting the hard chromium electroplating liquid medicine blending scheme and transmitting the hard chromium electroplating liquid medicine blending scheme to the server, the step of outputting the alkali copper liquid medicine blending scheme and transmitting the alkali copper liquid medicine blending scheme to the server, the step of outputting the nickel liquid medicine blending scheme and transmitting the nickel liquid medicine blending scheme to the server, and the step of outputting the acid copper liquid medicine blending scheme and transmitting the acid.
Step S12: and the mobile terminal receives the deployment scheme of the server.
The method for preparing the electroplating solution provided by the embodiment can be implanted into WeChat small programs, and has a wide application range. The mobile terminal logs in to the small program through the two-dimensional code generated by the small program scanned by the WeChat, and meanwhile, the ID identification information of the WeChat user is stored in the server; after the user logs in, the user selects the electroplating process required to be adjusted and clicks to enter a related page; inputting the current content of each component in the electroplating liquid medicine, calculating by clicking, and obtaining the specific process adjustment scheme of the electroplating liquid medicine by calculating according to relevant conditions.
The method for allocating the electroplating liquid medicine provided by the embodiment avoids the loss possibly caused by the calculation and adjustment error of workshop operators, improves the production efficiency of workshop workers, enables a user to use the mobile terminal to analyze the components of the electroplating liquid medicine, inputs the current content of each component of the electroplating liquid medicine, calculates and analyzes through the system, obtains a proper electroplating process adjustment scheme, and provides convenience for the user.
The method for preparing the electroplating solution provided by the embodiment has the advantages that the preparation steps are simple, the stability of the electroplating solution is high, the problem of electroplating solution loss caused by a preparation error is solved, and the production efficiency is improved.
Referring to fig. 5, in an alternative embodiment of the present application, there is provided a system for dispensing electroplating solution, including:
the mobile terminal S601 is used for scanning the two-dimensional code generated by the WeChat applet through WeChat so as to log in the WeChat applet; selecting an electroplating liquid medicine page needing to be prepared, obtaining the current content of each component in the electroplating liquid medicine, and transmitting the current content of each component in the electroplating liquid medicine to a calculator S602.
And the calculator S602 is used for comparing the current content of each component in the electroplating liquid medicine with a standard data range respectively, and outputting a blending scheme to the server S603 according to the result of comparison.
The server S603 is configured to store the identification information of the user ID of the wechat, receive the provisioning scheme from the calculator S602, and transmit the provisioning scheme to the mobile terminal S601.
The system for allocating electroplating solution provided by the embodiment can realize the other method for allocating electroplating solution, has simple allocation steps and high stability of electroplating solution, can not generate the problem of electroplating solution loss caused by allocation errors, and improves the production efficiency.
Finally, it should also be noted that, herein, relational terms such as first and second, and the like may be 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 phrase "comprising an … …" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
The method, apparatus, system, computing device and storage medium for dispensing electroplating solution provided by the present invention are described in detail above, and the principle and implementation of the present invention are explained herein by applying specific examples, and the description of the above examples is only used to help understand the method and core ideas of the present invention; meanwhile, for a person skilled in the art, according to the idea of the present invention, there may be variations in the specific embodiments and the application scope, and in summary, the content of the present specification should not be construed as a limitation to the present invention.
Claims (10)
1. A method for preparing electroplating liquid medicine is applied to gravure plate-making industry, and is characterized by comprising the following steps:
obtaining the current content of each component in the electroplating liquid medicine;
grouping the components;
comparing the current content of each component in each group with a standard data range;
and outputting each group of allocation schemes according to the result of the larger value and the smaller value.
2. The method of dispensing an electroplating bath as claimed in claim 1, wherein:
the current content of each component in the electroplating liquid medicine is obtained, and the current content of each component in the electroplating hard chromium liquid medicine is obtained, wherein each component in the electroplating hard chromium liquid medicine comprises chromic anhydride, sulfuric acid, trivalent chromium and chloride ions;
said grouping said components comprises grouping said components into three groups, said chromic anhydride and sulfuric acid being a first group, said trivalent chromium being a second group, said chloride ions being a third group;
said comparing the current content of said ingredients within each group to a standard data range respectively comprises comparing chromic anhydride and sulfuric acid in said first group to chromic anhydride and sulfuric acid in said standard data range respectively, comparing trivalent chromium in said second group to trivalent chromium in said standard data range, and comparing chloride ions in said third group to chloride ions in said standard data range;
and outputting each group of allocation schemes according to the result of the larger value, wherein the outputting comprises outputting a first group of allocation schemes, outputting a second group of allocation schemes and outputting a third group of allocation schemes.
3. The method of claim 1, wherein obtaining the current content of each component in the electroplating bath comprises obtaining the current content of each component in an alkaline copper bath, wherein each component in the alkaline copper bath comprises copper ions and a pH;
the grouping of the components comprises dividing the components into two groups, wherein the copper ions are in a fourth group, and the pH value is in a fifth group;
comparing the current content of each component in each group with a standard data range, respectively, comprising comparing copper ions in the fourth group with copper ions in the standard data range, and comparing pH values in the fifth group with pH values in the standard data range;
and outputting each group of blending schemes according to the result of the larger value and the smaller value, wherein the step of outputting the fourth group of blending schemes and the step of outputting the fifth group of blending schemes are included.
4. The method of claim 1, wherein obtaining the current content of each component in the electroplating bath comprises obtaining the current content of each component in a nickel bath comprising nickel sulfate, nickel chloride, and boric acid;
the grouping of the components comprises grouping the components into three groups, wherein the nickel sulfate is a sixth group, the nickel chloride is a seventh group, and the boric acid is an eighth group;
said comparing the current content of said ingredients within each grouping to a standard data range respectively comprises comparing nickel sulfate in said sixth group to nickel sulfate in said standard data range, comparing nickel chloride in said seventh group to nickel chloride in said standard data range, comparing boric acid in said eighth group to boric acid in said standard data range;
and outputting each group of allocation schemes according to the result of the larger value, wherein the step of outputting each group of allocation schemes comprises outputting a sixth group of allocation schemes, outputting a seventh group of allocation schemes and outputting an eighth group of allocation schemes.
5. The method of claim 1, wherein obtaining the current content of each component in the electroplating bath comprises obtaining the current content of each component in a copper acid bath, wherein each component in the copper acid bath comprises copper sulfate, sulfuric acid, and chloride ions;
the grouping of the components comprises grouping the components into three groups, wherein the copper sulfate is a ninth group, the sulfuric acid is a tenth group, and the chloride ions are the tenth group;
said comparing the current content of said ingredients within each group to a standard data range respectively comprises comparing copper sulfate in said ninth group to copper sulfate in said standard data range, comparing sulfuric acid in said tenth group to sulfuric acid in said standard data range, comparing chloride ions in said tenth group to chloride ions in said standard data range;
and outputting each group of blending schemes according to the result of the larger value, wherein the step of outputting each group of blending schemes comprises outputting a ninth group of blending schemes, outputting a tenth group of blending schemes and outputting an eleventh group of blending schemes.
6. The utility model provides a device of allotment electroplating solution, is applied to in the gravure plate-making trade, its characterized in that includes:
the acquisition module is used for acquiring the current content of each component in the electroplating liquid medicine;
the grouping module is used for grouping the components;
the comparison module is used for comparing the current content of each component in each group with a standard data range;
and the output module is used for outputting the allocation scheme of each group according to the result of the larger value and the smaller value.
7. The apparatus for dispensing electroplating bath solution of claim 6, wherein:
the obtaining module comprises a first obtaining unit, wherein the first obtaining unit is used for obtaining the current content of each component of the hard chromium electroplating liquid medicine, and each component of the hard chromium electroplating liquid medicine comprises chromic anhydride, sulfuric acid, trivalent chromium and chloride ions;
the grouping module comprises a first grouping unit for grouping the components into three groups, the chromic anhydride and sulfuric acid being a first group, the trivalent chromium being a second group, and the chloride ions being a third group;
the comparison module comprises a first comparison unit for comparing chromic anhydride and sulfuric acid in the first set with chromic anhydride and sulfuric acid in the standard data range, respectively, trivalent chromium in the second set with trivalent chromium in the standard data range, and chloride ions in the third set with chloride ions in the standard data range;
the output module comprises a first output unit, and the first output unit is used for outputting a first group of blending schemes, outputting a second group of blending schemes and outputting a third group of blending schemes.
8. The apparatus for dispensing electroplating bath solution of claim 6, wherein:
the acquisition module comprises a second acquisition unit, and the second acquisition unit is used for acquiring the current content of each component of the alkali copper liquid medicine, wherein each component of the alkali copper liquid medicine comprises copper ions and a pH value;
the grouping module comprises a second grouping unit, the second grouping unit is used for dividing the components into two groups, the copper ions are in a fourth group, and the pH value is in a fifth group;
the comparison module comprises a second comparison unit for comparing the copper ions in the fourth group with the copper ions in the standard data range, and for comparing the pH values in the fifth group with the pH values in the standard data range;
the output module comprises a second output unit, and the second output unit is used for outputting the fourth group of blending schemes and outputting the fifth group of blending schemes.
9. The apparatus for dispensing electroplating bath solution of claim 6, wherein:
the acquisition module comprises a third acquisition unit, wherein the third acquisition unit is used for acquiring the current content of each component of the nickel liquid medicine, and each component of the nickel liquid medicine comprises nickel sulfate, nickel chloride and boric acid;
the grouping module comprises a third grouping unit, wherein the third grouping unit is used for grouping the components into three groups, the nickel sulfate is a sixth group, the nickel chloride is a seventh group, and the boric acid is an eighth group;
the comparison module comprises a third comparison unit for comparing the nickel sulfate in the sixth group with the nickel sulfate in the standard data range, the nickel chloride in the seventh group with the nickel chloride in the standard data range, the boric acid in the eighth group with the boric acid in the standard data range;
the output module comprises a third output unit, and the third output unit is used for outputting a sixth group of blending schemes, outputting a seventh group of blending schemes and outputting an eighth group of blending schemes.
10. The apparatus for dispensing electroplating bath solution according to claim 6,
the acquisition module comprises a fourth acquisition unit, and the fourth acquisition unit is used for acquiring the current content of each component of the acid copper liquid medicine, wherein each component of the acid copper liquid medicine comprises copper sulfate, sulfuric acid and chloride ions;
the grouping module comprises a fourth grouping unit for grouping the components into three groups, the copper sulfate is a ninth group, the sulfuric acid is a tenth group, and the chloride ions are the tenth group;
the comparison module comprises a fourth comparison unit for comparing copper sulfate in the ninth group with copper sulfate in the standard data range, sulfuric acid in the tenth group with sulfuric acid in the standard data range, and chloride ions in the tenth group with chloride ions in the standard data range;
the output module comprises a fourth output unit, and the fourth output unit is used for outputting a ninth group of blending schemes, outputting a tenth group of blending schemes and outputting an eleventh group of blending schemes.
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| CN201811018337.XA CN110872724A (en) | 2018-09-03 | 2018-09-03 | Method and device for preparing electroplating liquid medicine |
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