CN115233283A - Metal surface cleaning agent - Google Patents

Metal surface cleaning agent Download PDF

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Publication number
CN115233283A
CN115233283A CN202210963879.4A CN202210963879A CN115233283A CN 115233283 A CN115233283 A CN 115233283A CN 202210963879 A CN202210963879 A CN 202210963879A CN 115233283 A CN115233283 A CN 115233283A
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metal
polishing
pulse
cleaning agent
power supply
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梁嘉晟
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Wuxi Jizhi Electronic Technology Co ltd
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Wuxi Jizhi Electronic Technology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F3/00Electrolytic etching or polishing
    • C25F3/16Polishing
    • C25F3/18Polishing of light metals
    • C25F3/20Polishing of light metals of aluminium
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F3/00Electrolytic etching or polishing
    • C25F3/16Polishing
    • C25F3/22Polishing of heavy metals
    • C25F3/24Polishing of heavy metals of iron or steel
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F3/00Electrolytic etching or polishing
    • C25F3/16Polishing
    • C25F3/22Polishing of heavy metals
    • C25F3/26Polishing of heavy metals of refractory metals
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F7/00Constructional parts, or assemblies thereof, of cells for electrolytic removal of material from objects; Servicing or operating

Abstract

The invention provides a metal surface cleaning agent which is composed of polyol, perchloric acid, polyalcohol amine, sulfydryl sulfonyl ionic compounds and pyridinium salt compounds, and can effectively obtain a metal surface with low roughness, high flatness and high glossiness under the conditions of a direct current power supply and a pulse power supply.

Description

Metal surface cleaning agent
Technical Field
The invention designs a cleaning agent for a metal surface, and particularly relates to the field of cleaning of an aluminum alloy surface.
Technical Field
In nature, aluminum is the metal element with the highest content, the occupied shell content is 8.3, the aluminum and aluminum alloy products have the advantages of small specific gravity, good electric and thermal conductivity, high specific strength, high temperature resistance, various medium corrosion resistance, fatigue resistance, good light and heat reflection performance and the like, are typical light alloy materials, are widely applied to the civil field, the building field, the mechanical manufacturing field, the scientific and technological field, the military field, the electronic and electrical field, the transportation field, the aerospace field, the chemical industry field and the like, and the continuous development of scientific technology and industrial technology provides higher requirements and standards for the surface quality of aluminum and aluminum alloy workpieces, particularly for the two aspects of the surface glossiness and the flatness of the workpieces, so that the aluminum and aluminum alloy workpieces can meet the use standards of industrial production and life, and the surfaces of the aluminum and aluminum alloy workpieces usually achieve the decorative effect of sand surfaces or mirror surfaces.
However, aluminum and aluminum alloy have low hardness and poor wear resistance, and aluminum alloy materials cause mechanical damage to workpieces during manufacturing and production, and generate defects such as pores, scratches, bruises, scratches and abrasion on the surfaces of aluminum and aluminum alloy workpieces. Due to the existence of the surface defects, the appearance and application value of the aluminum and aluminum alloy workpiece are greatly influenced, the surface smoothness and brightness of the aluminum and aluminum alloy workpiece are reduced, and the existence of the defects particularly influences the chemical stability of the workpiece, particularly obviously influences the corrosion resistance, local corrosion is often generated preferentially at the surface defects of the workpiece, and the service time of the workpiece is greatly shortened. Therefore, solving the problem of surface defects of aluminum and aluminum alloy products is a central focus of the continued development of the aluminum and aluminum alloy industry. To eliminate these surface defects and achieve high surface brightness and good decorative effect, aluminum and aluminum alloy workpieces are usually subjected to surface treatment.
Polishing techniques can be classified into mechanical polishing, electrochemical polishing (electropolishing), and chemical polishing according to their principles of action and process characteristics. The surface polishing treatment technology can be used for final treatment of the surface of an aluminum and aluminum alloy workpiece, and can also be used as a pretreatment process of anodic oxidation and electroplating of the aluminum and aluminum alloy. Each polishing method has the advantages and disadvantages of the polishing methods, different polishing modes are selected, and the polishing effects of the treated aluminum and the treated aluminum alloy are different, which are mainly reflected in four aspects of polishing process, polishing cost, workpiece surface finish and influence on atmospheric environment.
The mechanical polishing is that under the action of external force, the very fine polishing paste smeared on a polishing disc and the surface of a workpiece to be processed are ground and rolled, and the convex part of the processed surface of the workpiece is removed, so that the uneven surface becomes flat and smooth. However, in the mechanical polishing process, the surface of the workpiece is affected by the factors such as extrusion and heat, a new crystal deformation layer is formed on the surface of the workpiece, the surface structure of the workpiece is damaged, and the polished aluminum alloy workpiece still has problems and cannot meet the use requirements of products, such as insufficient surface smoothness of the polished workpiece, poor corrosion resistance and easy generation of stress corrosion or grain boundary corrosion. Although the surface of the workpiece after mechanical polishing can be sufficiently flat and bright, if such a workpiece is directly subjected to the anodic oxidation process, a high-quality film excellent in decorative effect cannot be obtained. In addition, mechanical polishing can only perform polishing treatment on some workpieces with simple appearance structures, and for decorative materials, precise parts and optical parts which have high requirements on the surface performance of the workpieces and have complex shapes, the mirror reflectivity and the surface flatness required by the workpieces cannot be achieved by only depending on mechanical polishing.
For example, CN105081941A discloses a mechanical polishing process for the inner wall of a stainless steel storage tank, which comprises the following steps:
1) Rough polishing: grinding, polishing or lapping the surface of a workpiece by using 60# to 100# carborundum wheels to remove burrs, scratches, rust marks, oxide skin, welding bead excess height, welding beading, welding slag and the like on the surface, removing a surface oxide layer and exposing metallic luster;
2) Fine polishing: further processing the roughly polished surface by adopting an 80# carborundum grinding wheel and a thousand-blade wheel, removing scratches left during rough polishing, and generating a smooth to medium-brightness surface;
3) Fine polishing: polishing the surface of the stainless steel storage tank by adopting a 240# -320 # fiber wheel and a cloth wheel coated with polishing paste, further reducing the roughness of the surface of the stainless steel, and achieving the purpose of micro-leveling;
4) And (3) polishing detection: and (3) detecting by adopting a center line average value method, transversely moving the roughness detector on the surface of the stainless steel storage tank during detection, and recording the peak-valley variation amplitude.
Chemical polishing and electrochemical polishing are similar, and rely on the etching action of special chemical reagents to the surface of a workpiece
Selectively dissolving the rugged region, and under the condition of a certain temperature and time, etching off the oxide layer and the crystal deformation layer on the surface, thereby eliminating the grinding marks on the surface and leveling the etching. The surface glossiness of the workpiece after chemical polishing is improved, the surface roughness is reduced, the chemical stability is improved, the light and heat reflecting capacity is enhanced, and the like. But compared with electrochemical polishing, the chemical polishing has the advantages of less equipment fund, no need of power supply equipment and corresponding clamps, simple equipment, simple operation, high production efficiency, capability of effectively processing parts which are thin tubes, have deep holes, and have small sizes and complex shapes. Because most of aluminum and aluminum alloys have no special requirements in use occasions, the requirements of daily industry and life on the surface glossiness and the flatness can be met, and the chemical polishing process is completely sufficient. The chemical polishing is suitable for the aluminum and aluminum alloy products, other products such as copper, nickel, titanium and alloy products thereof, and even workpieces comprising steel, silver and the like, and can improve the smoothness of the surface of the material by using a chemical polishing process or an electrochemical polishing process.
For example, CN102277575A discloses a chemical polishing solution for aluminum products and a preparation method thereof, relating to a chemical polishing solution. The nitrate-modified 'triacid' polishing process has the advantages of less yellow smoke, low pollution, no nitric acid and the like, the polishing quality can reach the level of the traditional 'triacid' process, and the chemical polishing solution for the aluminum products and the preparation method thereof can reduce the environmental pollution caused by the release of nitrogen oxides. The raw materials of the coating comprise sulfuric acid, phosphoric acid, boric acid, a passivating agent, a fog-inhibiting brightener, citric acid, tartaric acid and water. The method comprises the specific steps of adding all solid raw materials into water, adding phosphoric acid and sulfuric acid in sequence after dissolving, and transferring the solution into a volumetric flask for constant volume after cooling. The using method comprises the following steps: heating the chemical polishing solution of the aluminum product to 95-110 ℃; immersing the dried and clean aluminum product to be polished into the chemical polishing solution of the aluminum product, and taking out after processing for 30-100 s; and immersing the taken aluminum product to be polished into nitric acid for brightening for 25-120 s, and cleaning to finish polishing the aluminum product.
Electrochemical polishing (also called electropolishing) refers to a surface finishing technique in which the anode of a metal workpiece is dissolved in a certain electrolyte to reduce the surface roughness and improve the brightness of the metal workpiece, thereby producing a certain metal luster. The specific process is as follows: the workpiece to be treated is taken as an anode, insoluble metal is taken as a cathode (a lead plate or a stainless steel plate is mostly adopted), then a cathode and an anode are placed in electrolytic bath solution, a direct current power supply is turned on to start polishing, and the anode which is selective to the surface of the aluminum and aluminum alloy workpiece is dissolved in the polishing process, so that the surface of the workpiece with higher glossiness and smoother surface is obtained. Electrochemical polishing techniques have been developed over decades to improve the properties of metal surfaces without changing the properties of the bulk of the workpiece. Metals and alloys become more flat, smooth, and more corrosion resistant after electrochemical polishing, which dissolves particles produced by mechanical polishing.
For example, CN110846710A discloses an electrochemical polishing method for the surface of copper material, comprising the following steps: preparing a polishing solution; soaking a copper material to be polished into a polishing solution, and turning on a power supply to polish; wherein, preparing the polishing solution comprises: calculating the dosage of each solute according to the total volume of the solution to be prepared, wherein the solutes comprise phosphoric acid, glycerol, thiourea and polyoxyethylene alkanolamide; according to the calculation result, weighing phosphoric acid and glycerol, introducing the phosphoric acid and the glycerol into a corrosion-resistant container, adding water until the total volume is reached, and stirring and dissolving to obtain a first intermediate solution; according to the calculation result, weighing thiourea, adding the thiourea into the first intermediate solution, and stirring and dissolving to obtain a second intermediate solution; and measuring polyoxyethylene alkanolamide according to the calculation result, adding the polyoxyethylene alkanolamide into the second intermediate solution, and uniformly stirring to obtain the polishing solution. The invention can improve the surface roughness of the copper precision part from Ra0.4 mu m to Ra0.2 mu m so as to meet the use requirement of a vacuum electronic device.
Compared with chemical polishing and mechanical polishing, the electrochemical polishing has the advantages that (1) high surface smoothness can be obtained; (2) high polishing precision can be obtained; (3) the operation environment is good, and the metal loss is small; (4) the energy consumption is low; (5) can process workpieces of any shape and size; (6) the polishing speed is independent of the physical and mechanical properties of the metal; (7) the production efficiency can be greatly improved; (g) The physical and mechanical properties, the physical and chemical properties and the service performance of the surface of the metal part can be improved; (9) the operation technology is easy to master; (10) the application range is wide.
Disclosure of Invention
Based on the introduction of polishing, the invention provides the metal surface cleaning agent which is used as an electrochemical polishing electrolyte, can effectively polish a metal substrate, and can obtain a metal surface with low roughness, high flatness, good corrosion resistance and good stability.
The metal surface cleaning agent consists of polyol, perchloric acid, polyol amine, mercapto sulfonyl ionic compound and pyridinium salt compound.
The polyalcohol is one of dipropylene glycol, glycerol or butanediol.
The polyalcohol amine is selected from one of diisopropanolamine, triisopropanolamine or triethanolamine.
The sulfydryl sulfonyl ionic compound is selected from one of thiazolinyl dithio propane sodium sulfonate, dimethyl dithio carbonyl propane sodium sulfonate and 3- (benzothiazole-2-sulfydryl) -propane sodium sulfonate.
The pyridinium salt compound is one selected from 1-ethyl-3-methylpyridinium bis (trifluoromethylsulfonyl) imide, 3- (4-tert-butyl 1-pyridyl) propanesulfonate or 3- (1-pyridyl) propanesulfonate.
Further, the content of the polyol is 30-65vol.%, the content of the perchloric acid is 3-5vol.%, the content of the polyalcohol amine is 10-15ml/L, the content of the mercapto sulfonyl ionic compound is 3-5g/L, and the content of the pyridinium salt compound is 1.5-3g/L.
Further, the metal is stainless steel, aluminum alloy or titanium alloy, preferably aluminum alloy.
Furthermore, the metal is used as an anode, the inert metal is used as a cathode, the cleaning agent is used as electrolyte, and a power supply is applied between the metal and the inert technology to clean the anode metal.
Further, the power supply is a direct-current power supply firstly and then a pulse power supply, and the pulse is a millisecond pulse firstly and then a microsecond pulse secondly.
Further, the preparation method of the cleaning agent comprises the following steps:
(1) Mixing polyalcohol amine and polyalcohol at 5-10 deg.C, and stirring;
(2) Continuously stirring, keeping the temperature stable, slowly adding perchloric acid, and uniformly stirring;
(3) Continuously stirring, simultaneously adding the sulfydryl sulfonyl ionic compound and the pyridinium salt compound, slowly heating to the normal temperature, and continuously stirring for 1-2h to obtain the cleaning agent.
Taking the metal as an anode, taking the inert metal as a cathode and taking the cleaning agent as electrolyte, and applying a power supply between the metal anode and the inert metal cathode to clean the metal of the anode;
the cleaning process comprises the following steps:
(1) Starting a direct current power supply: the current density is 3-5A/cm 2 Polishing for 5-7min at 20-25 deg.C and a polar distance of 15-20mm;
(2) Intermittent step: turning off the power supply, and turning on stirring at the speed of 200-300rpm and the temperature of 17-23 deg.C for 2-3min.
(3) Turning on a millisecond pulse power supply: the forward pulse current density is 2-3mA/cm 2 The forward pulse width is 100-150ms, the forward duty ratio is 10-15%, the pulse number is 5-10, and the reverse pulse current density is 2-3mA/cm 2 Pulse width is 150-170ms, reverse duty ratio is 10-15%, pulse number is 1, temperature is 20-25 ℃, time is 2-3min;
(4) Intermittent step: turning off the power supply, and turning on stirring at the speed of 200-300rpm and the temperature of 17-23 deg.C for 2-3min.
(5) Turning on a microsecond pulse power supply: the forward pulse current density is 1-2mA/cm 2 The forward pulse width is 50-100 mus, the forward duty ratio is 10-15%, the pulse number is 10-15, the reverse pulse current density is 1-2mA/cm < 2 >, the reverse pulse width is 50-100 mus, the reverse duty ratio is 10-15%, the pulse number is 1, the temperature is 13-15 ℃, and the time is 0.5-1min.
(6) And (3) post-treatment: turning off the power supply, washing with absolute ethyl alcohol, purging and drying in inert atmosphere of nitrogen or argon at 35-40 deg.C for 1-2h.
The cleaning solution of the present invention is composed of polyol, perchloric acid, polyalcohol amine, sulfydryl sulfonyl ionic compound, pyridinium salt compound, and the balance is made up by deionized water, and is a standard deionized water cleaning system, generally speaking, the components of the polishing solution are relatively complex, and the types of the polishing solutions suitable for each material are different, and no definite formula is provided, and most of the polishing solutions need to be tested and searched, but the types of the components are roughly divided into three parts, namely, polishing base solution, oxidant and various additives, the oxidant is the most important component, and the electrochemical polishing solution mainly comprises three main types, namely, acid-acid systems, such as concentrated sulfuric acid-concentrated phosphoric acid; acid-alcohol systems, such as concentrated sulfuric acid-methanol/ethanol, and the like; alcohol-salt systems, such as glycol-chloride salts, and the like. Each polishing solution system cannot meet all requirements, has certain advantages and disadvantages, and does not have a completely ideal polishing solution system. Acid-acid systems mostly adopt strong acid, such as concentrated sulfuric acid, concentrated phosphoric acid and the like, and although the polishing quality is good and the polishing efficiency is high, the corrosivity is strong, the reaction process is not easy to control, and the use process is easy to cause danger. In an acid-alcohol system, alcohol is generally volatile and is not easy to store, and the alcohol and the acid are easy to react to generate lipid, so that the operation process has high requirements on environment and the like. Although most of alcohol-salt systems have no pollution to the environment, the alcohol-salt systems have low polishing efficiency and high production cost due to low corrosivity and oxidation, and the polishing process has high requirements on polishing devices and the like. It can dissolve metal alloy, generate soluble salt and generate passive film on the surface of test piece. The polyhydric alcohol is used as a solvent to dissolve soluble salts generated by the anode, and simultaneously, carboxyl and hydroxyl contained in the soluble salts can play a corrosion inhibition role.
The polyalcohol and the polyalcohol amine are added simultaneously, the polyalcohol amine is selected from one of diisopropanolamine, triisopropanolamine or triethanolamine, the polyalcohol amine is alkalescent and can be a complexing agent or a leveling agent, and mucosa can be generated on the surface and adsorbed on the surface to help polishing and gradually flatten the surface.
The composition of the mercapto sulfonyl ionic compound and the pyridinium salt compound has the technical effect of synergistic leveling and brightening, and the mercapto sulfonyl ionic compound is selected from one of thiazolinyl dithio propane sodium sulfonate, dimethyl dithio carbonyl propane sodium sulfonate and 3- (benzothiazole-2-mercapto) -propane sodium sulfonate; the pyridinium salt compound is one of 1-ethyl-3-methylpyridinium bis (trifluoromethylsulfonyl) imide, 3- (4-tert-butyl 1-pyridyl) propanesulfonate or 3- (1-pyridyl) propanesulfonate, and three pyridinium salt compounds have the following structural formulas:
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theoretically, in the metal polishing process, after the metal immersed in the electrolyte is electrified, electrons are lost at the anode, the metal is dissolved in the electrolyte in the form of ions, and the reaction formula is Al → 3Al 3+ +3e; in this process it is desirable that the aluminium ions leave the surface as quickly as possible; then, after the metal loses electrons, OH-ions do electromigration movement under the action of the electric field force, so that a large amount of local OH-ions are gathered near the metal anode to generate hydrolysis deposition reaction, namely Al is generated 3+ +3OH - →Al(OH) 3 Based on the theory that the pyridinium salts have a C = N structure and are amphiphilic compounds, one end of an anion can be adsorbed on the surface of an anode under the current condition to neutralize the anion in the anode, and metal ions such as aluminum ions released in the polishing and dissolving process can obviously form repulsion with nitrogen-containing positive charges to accelerate Al 3+ The metal ions enter into the electrolyte from the surface of the dissolved metal, and the rejected aluminum ions are very easy to hydrolyze with water to form hydroxide particles, which affect the polishing effect, and in order to prevent excessive hydrolysis of the aluminum ions, the metal ions (Al) entering into the solution 3+ ) Can be combined with C-S = O and N = C-S in the sulfydryl sulfonyl group, the unshared electron pair in the functional group is filled in the empty orbit of the metal ion to realize the strong adsorption effect with the metal ion and further avoid the deposition of the metal, in addition, the sulfydryl sulfonyl ion type compound and the pyridinium salt type compound have rich ring structures, the adsorption conjugation effect is obvious, a mucosa structure is formed on the surface, the rapid corrosion of the convex part and the slow corrosion of the concave part are controlled, and the leveling is finally obtainedThe brightening effect is not limited by the two, if pyridinium salts are lacked, metal ions can not effectively move and diffuse away from the metal surface, and if mercapto sulfonyl ionic compounds are lacked, the metal ions can not effectively avoid hydrolysis, as shown in attached figures 1 and 2.
Another important reason for the excellent surface treatment effect obtained by the cleaning agent for treating the metal surface is the electrochemical electrolysis parameter, the electrochemical polishing power supply mainly adopted in the prior art is a direct current power supply or a pulse power supply, a direct current-pulse treatment mode is adopted, and a millisecond-level-first and micron-level-second electrochemical treatment process is adopted.
The method comprises the steps of taking a base material to be treated as an anode, adding the cleaning agent prepared in the preparation process, and then performing anodic electrochemical polishing, wherein the metal to be treated is stainless steel, aluminum alloy or titanium alloy, preferably aluminum alloy, and the metal can be subjected to various surface pretreatments including but not limited to oil removal and degreasing, acid pickling and activation, sand blasting, grinding, polishing and the like.
The method comprises the steps of firstly carrying out direct-current electrolytic polishing on a substrate, wherein in the initial stage of the direct-current electrolytic polishing, due to the fact that the roughness degrees of the surfaces of parts are different, namely, the roughness of the metal surface is staggered, electrolyte is adsorbed on the metal surface and oxidation reaction occurs, a viscous liquid film generated at a convex part is smaller than the thickness of the viscous liquid film generated at a concave part, the viscous liquid film at the convex part is greatly impacted by power lines and stirred by liquid, and in addition, the convex part is closer to a cathode, the electric field intensity is large, electrons are easily lost according to the principle of point discharge, and positive charges are highly concentrated at the convex part. Since the anions around the anode preferentially react with the cations at the protrusions, the metal forming the protrusions dissolves at a faster rate than the depressions. For direct current electrolytic polishing, the obvious concave-convex structure existing on the metal surface has obvious and faster flattening effect, the whole process is rough and fast, and although the direct current electrolytic polishing is not fine, the efficiency is faster, as shown in figure 3.
Direct current electrolysis conditions: the current density is 3-5A/cm 2 Polishing at 20-25 deg.C for 5-7min15-20mm; wherein, the current density has the biggest influence on the DC electrolytic polishing process and is the energy source for polishing. Too large or too small a current density can adversely affect polishing. When the current density is too small, the polished surface is always in a dissolving stage, the surface roughness is large, no metal luster exists, and the polishing effect is small. Too high a current density results in violent reaction, more heat generation and perchloric acid
The oxidation property is enhanced along with the rise of the temperature, the surface material is more corroded and removed, and the surface brightness is enhanced. Meanwhile, oxygen precipitation on the surface of the anode is increased, and the phenomena of uneven polishing and excessive polishing of the surface can occur due to the stirring of gas. In addition, the inter-electrode distance during electrochemical polishing is larger than that during electrolytic machining, and the purpose of ensuring more uniform dissolution of metal in the polishing process is mainly achieved, so that a better polishing effect is achieved. When the interelectrode distance is too small, the diffusion of the reactant is inconvenient, the temperature of the polishing solution rises quickly, and the heat dissipation is poor. When the interelectrode distance is too large, the current density is reduced, the polishing effect is not obvious, and the final optimized reaction condition is that the current density is 3-5A/cm 2 The polishing time is 5-7min, the temperature is 20-25 ℃, the inter-polar distance is 15-20mm, and compared with pulse electrolysis, the direct current electrolytic polishing has the advantages of large current density, long time and capability of quickly obtaining a flat surface.
The roughness of the metal surface treated by direct current electrolytic polishing is about 5-10 μm, the polishing precision is obviously insufficient, the main reasons may be that the direct current voltage is constant, the removal of polishing products and heat is difficult, and the products are accumulated on the surface of the anode, so that the roughness of the surface of a workpiece is increased, and further the surface quality is poor.
Then, pulse processing is carried out:
(2) Turning on a millisecond pulse power supply: the forward pulse current density is 2-3mA/cm 2 The forward pulse width is 100-150ms, the forward duty ratio is 10-15%, the pulse number is 5-10, and the reverse pulse current density is 2-3mA/cm 2 The pulse width is 150-170ms, the reverse duty ratio is 10-15%, the pulse number is 1, the temperature is 20-25 ℃, and the time is 2-3min.
(3) Intermittent step: turning off the power supply, and turning on stirring at the speed of 200-300rpm and the temperature of 17-23 deg.C for 2-3min.
(4) Turning on a microsecond pulse power supply: the forward pulse current density is 1-2mA/cm 2 The forward pulse width is 50-100 mus, the forward duty ratio is 10-15%, the pulse number is 10-15, the reverse pulse current density is 1-2mA/cm < 2 >, the reverse pulse width is 50-100 mus, the reverse duty ratio is 10-15%, the pulse number is 1, the temperature is 13-15 ℃, and the time is 0.5-1min.
Compared with direct current chemical polishing, the surface roughness of the polished surface of the pulse current electrochemical polishing is greatly reduced, and theoretically, pressure waves can be generated in the electrode gap at the moment of electrifying, bubbles can be generated in the electrode gap due to the action of the pressure waves, and the surface of the anode is corroded. At the moment of power failure, the bubbles are suddenly expanded and merged, and the anode product is flushed and rolled away, so that the phenomenon of surface roughness deterioration caused by the fact that the surface product cannot be removed in time is effectively reduced. Generally, the narrower the pulse width of the pulse current, the higher the frequency, and the more advantageous the convection field improvement, because the smaller the pulse width, the higher the frequency, the faster the electrolyte renewal speed in the gap, and the more obvious the impact effect of the pressure wave, and the more advantageous the surface quality improvement.
Based on the consideration, the invention adopts a periodic reversing pulse power supply, the periodic reversing pulse is formed by adding one or more reverse pulses after a group of forward pulses, the migration of an anode product can be further accelerated, and further high polishing effect can be obtained, in the pulse stage, firstly, relatively high current is used for carrying out millisecond-level anode polishing for a long time, the obtained metal surface roughness is about 400-600nm, then, relatively low current is used for carrying out microsecond-level anode polishing for a short time, the obtained metal surface roughness is about 50-150nm, compared with the mode of directly carrying out microsecond-level periodic reversing pulse electrochemical treatment, the same polishing effect can be obtained, the 3/4 polishing time can be shortened, the polishing effect is greatly satisfied, and the polishing effect is shown in figure 4.
Advantageous technical effects
(1) The invention effectively prepares the cleaning solution, particularly the sulfydryl sulfonyl ionic compound and the pyridinium salt compound, and has direct influence on the roughness, high flatness and glossiness of the metal surface treatment.
(2) According to the invention, the metal surface is treated by direct current, millisecond pulse and microsecond pulse, so that the working hour consumption is effectively reduced and the loss is reduced on the premise of ensuring low roughness, high gloss and low corrosion amount of the metal surface.
Drawings
FIG. 1 is a drawing of an aluminum alloy after treatment of comparative example 1 of the present invention.
FIG. 2 is a drawing of an aluminum alloy of comparative example 2 of the present invention after treatment.
FIG. 3 is a drawing of an aluminum alloy of comparative example 3 of the present invention after treatment.
FIG. 4 is a drawing of an aluminum alloy after treatment in example 2 of the present invention.
Detailed Description
Example 1
The metal surface cleaning agent consists of polyol, perchloric acid, polyol amine, a sulfydryl sulfonyl ionic compound and a pyridinium salt compound, wherein the content of the polyol is 30vol.%, the content of the perchloric acid is 3vol.%, the content of the polyol amine is 10ml/L, the content of the sulfydryl sulfonyl ionic compound is 3g/L, the content of the pyridinium salt compound is 1.5g/L, and the balance is deionized water.
The polyol is selected from dipropylene glycol.
The polyalcohol amine is selected from diisopropanolamine.
The mercapto sulfonyl ionic compound is selected from thiazolinyl dithio propane sodium sulfonate.
The pyridinium salt compound is selected from 3- (4-tertiary butyl 1-pyridyl) propane sulfonate.
And applying a power supply between the metal anode and the inert metal cathode to clean the anode metal by taking the metal as the anode, taking the inert metal as the cathode and taking the cleaning agent as electrolyte.
The cleaning process comprises the following steps:
(1) Starting a direct current power supply: current density 3A/cm 2 The polishing time is 5min, the temperature is 20 ℃, and the inter-polar distance is 15mm.
(2) Intermittent step: turning off the power supply, and turning on the stirring at the stirring speed of 200rpm and the stirring temperature of 17 ℃ for 2min.
(3) Turning on a millisecond pulse power supply: the forward pulse current density is 2mA/cm 2 The forward pulse width was 100ms, the forward duty ratio was 10%, the number of pulses was 5, and the reverse pulse current density was 2mA/cm 2 The pulse width is 150ms, the reverse duty cycle is 10%, the pulse number is 1, the temperature is 20 ℃, and the time is 2min.
(4) Intermittent step: turning off the power supply, and turning on the stirring at the stirring speed of 200rpm and the stirring temperature of 17 ℃ for 2min.
(5) Turning on a microsecond pulse power supply: the forward pulse current density is 1mA/cm 2 The forward pulse width was 50. Mu.s, the forward duty ratio was 10%, the pulse number was 10, and the reverse pulse current density was 1mA/cm 2 The pulse width is 50 mus, the forward duty ratio is 10%, the pulse number is 1, the temperature is 13 ℃, and the time is 0.5min.
The method comprises the following steps: turning off the power supply, washing with absolute ethyl alcohol, blowing and drying in inert atmosphere, wherein the inert atmosphere is nitrogen or argon, the temperature is 35 ℃, and the time is 1h.
Example 2
The metal surface cleaning agent consists of polyol, perchloric acid, polyol amine, a sulfydryl sulfonyl ionic compound and a pyridinium salt compound, wherein the content of the polyol is 55vol.%, the content of the perchloric acid is 4vol.%, the content of the polyol amine is 12.5ml/L, the content of the sulfydryl sulfonyl ionic compound is 4g/L, the content of the pyridinium salt compound is 2g/L, and the balance is deionized water.
The polyalcohol is one of glycerol.
The polyalcohol amine is one selected from triisopropanolamine.
The mercapto sulfonyl ionic compound is selected from one of dimethyl dithio carbonyl propane sodium sulfonate.
The pyridinium salt compound is selected from 1-ethyl-3-methylpyridinium bis (trifluoromethylsulfonyl) imide.
And applying a power supply between the metal anode and the inert metal cathode to clean the anode metal by taking the metal as the anode, taking the inert metal as the cathode and taking the cleaning agent as electrolyte.
The cleaning process comprises the following steps:
(1) Starting a direct current power supply: current density 4A/cm 2 The polishing time was 6min, the temperature 23 ℃ and the interpolar distance 17mm.
(2) Intermittent step: turning off the power supply, starting stirring at the speed of 250rpm and the temperature of 20 ℃ for 2.5min.
(3) Turning on a millisecond pulse power supply: the forward pulse current density is 2.5mA/cm 2 The forward pulse width was 125ms, the forward duty cycle was 12.5%, the pulse number was 8, and the reverse pulse current density was 2.5mA/cm 2 The reverse pulse width is 160ms, the reverse duty cycle is 12.5%, the pulse number is 1, the temperature is 23 ℃, and the time is 2.5min.
(4) Intermittent step: turning off the power supply, starting stirring at the speed of 250rpm and the temperature of 20 ℃ for 2.5min.
(5) Turning on a microsecond pulse power supply: the forward pulse current density is 1.5mA/cm 2 The forward pulse width was 75. Mu.s, the forward duty cycle was 12.5%, the pulse number was 13, the reverse pulse current density was 1.5mA/cm2, the reverse pulse width was 75. Mu.s, the reverse duty cycle was 12.5%, the pulse number was 1, the temperature was 14 ℃, and the time was 0.75min.
The method comprises the following steps: turning off the power supply, washing with absolute ethyl alcohol, blowing and drying in inert atmosphere, wherein the inert atmosphere is nitrogen or argon, the temperature is 38 ℃, and the time is 1.5h.
Example 3
The metal surface cleaning agent consists of polyol, perchloric acid, polyalcohol amine, sulfydryl sulfonyl ionic compounds and pyridinium compounds, wherein the content of the polyol is 65vol.%, the content of the perchloric acid is 5vol.%, the content of the polyalcohol amine is 15ml/L, the content of the sulfydryl sulfonyl ionic compounds is 5g/L, the content of the pyridinium compounds is 3g/L, and the balance is deionized water.
The polyhydric alcohol is selected from one of butanediol.
The polyalcohol amine is selected from one of triethanolamine.
The sulfydryl sulfonyl ionic compound is one of 3- (benzothiazole-2-sulfydryl) -propane sodium sulfonate.
The pyridinium salt compound is one selected from 3- (1-pyridyl) propanesulfonate.
Taking the metal as an anode, taking the inert metal as a cathode and taking the cleaning agent as electrolyte, and applying a power supply between the metal anode and the inert metal cathode to clean the anode metal; .
The cleaning process comprises the following steps:
(1) Starting a direct-current power supply: current density 5A/cm 2 The polishing time was 7min, the temperature was 25 ℃ and the interpolar distance was 20mm.
(2) Intermittent step: turning off the power supply, starting stirring at the speed of 300rpm and the temperature of 23 ℃ for 3min.
(3) Turning on a millisecond pulse power supply: the forward pulse current density is 3mA/cm 2 The forward pulse width was 150ms, the forward duty ratio was 15%, the pulse number was 10, and the reverse pulse current density was 3mA/cm 2 The pulse width is 170ms, the reverse duty cycle is 15%, the pulse number is 1, the temperature is 25 ℃, and the time is 3min.
(4) Intermittent step: turning off the power supply, and turning on stirring at the speed of 200-300rpm and the temperature of 17-23 deg.C for 2-3min.
(5) Turning on a microsecond pulse power supply: the forward pulse current density is 2mA/cm 2 The forward pulse width was 100. Mu.s, the forward duty ratio was 15%, the pulse number was 15, the reverse pulse current density was 2mA/cm2, the reverse pulse width was 100. Mu.s, the reverse duty ratio was 15%, the pulse number was 1, the temperature was 15 ℃, and the time was 1min.
The method comprises the following steps: turning off the power supply, washing with absolute ethyl alcohol, blowing and drying in inert atmosphere, wherein the inert atmosphere is nitrogen or argon, the temperature is 40 ℃, and the time is 2 hours.
Comparative example 1
The metal surface cleaning agent consists of polyol, perchloric acid and a polyol amine compound, wherein the polyol content is 55vol.%, the perchloric acid content is 4vol.%, the polyol amine content is 12.5ml/L, and the balance is deionized water.
The polyalcohol is one of glycerol.
The polyalcohol amine is one selected from triisopropanolamine.
The mercapto sulfonyl ionic compound is selected from one of dimethyl dithio carbonyl propane sodium sulfonate.
The pyridinium salt compound is selected from 1-ethyl-3-methylpyridinium bis (trifluoromethylsulfonyl) imide.
And applying a power supply between the metal anode and the inert metal cathode to clean the anode metal by taking the metal as the anode, taking the inert metal as the cathode and taking the cleaning agent as electrolyte.
The cleaning process comprises the following steps:
(1) Starting a direct current power supply: current density 4A/cm 2 The polishing time was 6min, the temperature 23 ℃ and the interpolar distance 17mm.
(2) Intermittent step: turning off the power supply, starting stirring at the speed of 250rpm and the temperature of 20 ℃ for 2.5min.
(3) Turning on a millisecond pulse power supply: the forward pulse current density is 2.5mA/cm 2 The forward pulse width was 125ms, the forward duty cycle was 12.5%, the pulse number was 8, and the reverse pulse current density was 2.5mA/cm 2 The reverse pulse width is 160ms, the reverse duty cycle is 12.5%, the pulse number is 1, the temperature is 23 ℃, and the time is 2.5min.
(4) Intermittent step: turning off the power supply, starting stirring at the speed of 250rpm and the temperature of 20 ℃ for 2.5min.
(5) Turning on a microsecond pulse power supply: the forward pulse current density is 1.5mA/cm 2 The forward pulse width was 75. Mu.s, the forward duty cycle was 12.5%, the pulse number was 13, the reverse pulse current density was 1.5mA/cm2, the reverse pulse width was 75. Mu.s, the reverse duty cycle was 12.5%, the pulse number was 1, the temperature was 14 ℃, and the time was 0.75min.
The method comprises the following steps: turning off the power supply, washing with absolute ethyl alcohol, blowing and drying in inert atmosphere, wherein the inert atmosphere is nitrogen or argon, the temperature is 38 ℃, and the time is 1.5h.
Comparative example 2
The metal surface cleaning agent consists of polyol, perchloric acid, polyalcohol amine and sulfydryl sulfonyl ionic compounds, wherein the content of the polyol is 55vol.%, the content of the perchloric acid is 4vol.%, the content of the polyalcohol amine is 12.5ml/L, the content of the sulfydryl sulfonyl ionic compounds is 4g/L, and the balance is deionized water.
The polyalcohol is one of glycerol.
The polyalcohol amine is one selected from triisopropanolamine.
The mercapto sulfonyl ionic compound is one selected from sodium dimethyl dithio carbonyl propane sulfonate.
And applying a power supply between the metal anode and the inert metal cathode to clean the anode metal by taking the metal as the anode, taking the inert metal as the cathode and taking the cleaning agent as electrolyte.
The cleaning process comprises the following steps:
(1) Starting a direct current power supply: current density 4A/cm 2 The polishing time was 6min, the temperature 23 ℃ and the interpolar distance 17mm.
(2) Intermittent step: turning off the power supply, starting stirring at the speed of 250rpm and the temperature of 20 ℃ for 2.5min.
(3) Turning on a millisecond pulse power supply: the forward pulse current density is 2.5mA/cm 2 The forward pulse width was 125ms, the forward duty cycle was 12.5%, the pulse number was 8, and the reverse pulse current density was 2.5mA/cm 2 The reverse pulse width is 160ms, the reverse duty cycle is 12.5%, the pulse number is 1, the temperature is 23 ℃, and the time is 2.5min.
(4) Intermittent step: turning off the power supply, starting stirring at the speed of 250rpm and the temperature of 20 ℃ for 2.5min.
(5) Turning on a microsecond pulse power supply: the forward pulse current density is 1.5mA/cm 2 The forward pulse width was 75. Mu.s, the forward duty cycle was 12.5%, and the pulse number was 13, the current density of the reverse pulse is 1.5mA/cm < 2 >, the width of the reverse pulse is 75 mus, the duty ratio of the reverse pulse is 12.5 percent, the pulse number is 1, the temperature is 14 ℃, and the time is 0.75min.
The method comprises the following steps: turning off the power supply, washing with absolute ethyl alcohol, purging and drying in inert atmosphere of nitrogen or argon at 38 ℃ for 1.5h.
Comparative example 3
The metal surface cleaning agent consists of polyol, perchloric acid, polyol amine, a sulfydryl sulfonyl ionic compound and a pyridinium salt compound, wherein the content of the polyol is 55vol.%, the content of the perchloric acid is 4vol.%, the content of the polyol amine is 12.5ml/L, the content of the sulfydryl sulfonyl ionic compound is 4g/L, the content of the pyridinium salt compound is 2g/L, and the balance is deionized water.
The polyalcohol is one of glycerol.
The polyalcohol amine is one selected from triisopropanolamine.
The mercapto sulfonyl ionic compound is selected from one of dimethyl dithio carbonyl propane sodium sulfonate.
The pyridinium salt compound is selected from 1-ethyl-3-methylpyridinium bis (trifluoromethylsulfonyl) imide.
And applying a power supply between the metal anode and the inert metal cathode to clean the metal anode by taking the metal as the anode, taking the inert metal as the cathode and taking the cleaning agent as electrolyte.
The cleaning process comprises the following steps:
(1) Starting a direct current power supply: current density 4A/cm 2 The polishing time is 10min, the temperature is 23 ℃, and the inter-polar distance is 17mm.
(2) And (3) post-treatment: turning off the power supply, washing with absolute ethyl alcohol, purging and drying in inert atmosphere of nitrogen or argon at 38 ℃ for 1.5h.
Comparative example 4
The metal surface cleaning agent consists of polyol, perchloric acid, polyol amine, a sulfydryl sulfonyl ionic compound and a pyridinium salt compound, wherein the content of the polyol is 55vol.%, the content of the perchloric acid is 4vol.%, the content of the polyol amine is 12.5ml/L, the content of the sulfydryl sulfonyl ionic compound is 4g/L, the content of the pyridinium salt compound is 2g/L, and the balance is deionized water.
The polyalcohol is one of glycerol.
The polyalcohol amine is one selected from triisopropanolamine.
The mercapto sulfonyl ionic compound is selected from one of dimethyl dithio carbonyl propane sodium sulfonate.
The pyridinium salt compound is selected from 1-ethyl-3-methylpyridinium bis (trifluoromethylsulfonyl) imide.
And applying a power supply between the metal anode and the inert metal cathode to clean the anode metal by taking the metal as the anode, taking the inert metal as the cathode and taking the cleaning agent as electrolyte.
The cleaning process comprises the following steps:
(1) Turning on a millisecond pulse power supply: the forward pulse current density is 2.5mA/cm 2 The forward pulse width was 125ms, the forward duty cycle was 12.5%, the pulse number was 8, and the reverse pulse current density was 2.5mA/cm 2 The reverse pulse width is 160ms, the reverse duty cycle is 12.5%, the pulse number is 1, the temperature is 23 ℃, and the time is 13min.
(2) Intermittent step: turning off the power supply, starting stirring at the speed of 250rpm and the temperature of 20 ℃ for 2.5min.
(3) Turning on a microsecond pulse power supply: the forward pulse current density is 1.5mA/cm 2 The forward pulse width was 75. Mu.s, the forward duty cycle was 12.5%, the pulse number was 13, the reverse pulse current density was 1.5mA/cm2, the reverse pulse width was 75. Mu.s, the reverse duty cycle was 12.5%, the pulse number was 1, the temperature was 14 ℃, and the time was 7.4min.
And (3) post-treatment: turning off the power supply, washing with absolute ethyl alcohol, blowing and drying in inert atmosphere, wherein the inert atmosphere is nitrogen or argon, the temperature is 38 ℃, and the time is 1.5h.
Surface roughness: respectively selecting 3 different regions on the surface of a sample by an RSE3000 surface roughness meter for detection, and averaging the roughness of the 3 regions to obtain a test result "
Surface glossiness: using aluminum material as sample, detecting and selecting 45 o The reflection angle, measured according to GB8807-88, is measured on the surface gloss of the test specimens.
TABLE 1
Figure DEST_PATH_IMAGE008
As shown in the above table, the roughness of the surface of the aluminum alloy obtained by the base solution + mercaptosulfonyl + pyridinium salt in the example 2 of the present invention is 53nm, the glossiness is 81.3%, and the corrosion amount of the product is small, in contrast, if the electrolyte is changed under the same electrolysis parameters, such as the mercaptosulfonyl + pyridinium salt in the comparative example 1 and the pyridinium salt in the comparative example 2, it can be seen that the electrolyte has a significant influence on the glossiness and the roughness of the product, which is ten times order of magnitude, and mainly the additive has a significant influence on the migration and diffusion of the generated oxidized particles in the electroplating solution. Comparative examples 3-4 are the same electrolyte, different electrolysis parameters, and if only direct current electrolysis is used, the polishing degree and the glossiness can not meet the requirements of low roughness and high metal luster in industry. The millisecond and microsecond pulse times of comparative example 3 were adjustable compared to directly pulsing, and by adjusting the time parameters of comparative example 3, a surface roughness effect consistent with example 2 was obtained. Although a high mirror effect can be obtained, the time consumption, the loss consumption, and the equipment load are significantly higher than those of embodiment 2 of the present invention.
Finally, it should be noted that the above embodiments are only intended to illustrate the technical solutions of the present invention and not to limit the same, and although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that modifications or equivalent substitutions may be made to the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention.

Claims (5)

1. A metal surface cleaning agent is characterized in that the surface cleaning agent consists of polyalcohol, perchloric acid, polyalcohol amine, sulfydryl sulfonyl ionic compound and pyridinium salt compound;
the polyalcohol is one of dipropylene glycol, glycerol or butanediol,
the polyalcohol amine is one of diisopropanolamine, triisopropanolamine or triethanolamine
The mercapto sulfonyl ionic compound is one of thiazolinyl dithio propane sodium sulfonate, dimethyl dithio carbonyl propane sodium sulfonate and 3- (benzothiazole-2-mercapto) -propane sodium sulfonate;
the pyridinium salt compound is one selected from 1-ethyl-3-methylpyridinium bis (trifluoromethylsulfonyl) imide, 3- (4-tert-butyl 1-pyridyl) propanesulfonate or 3- (1-pyridyl) propanesulfonate.
2. The metal surface cleaning agent according to claim 1, wherein the polyol is contained in an amount of 30 to 65vol.%, the perchloric acid is contained in an amount of 3 to 5vol.%, the polyalcohol amine is contained in an amount of 10 to 15ml/L, the mercapto sulfonyl ionic compound is contained in an amount of 3 to 5g/L, and the pyridinium salt compound is contained in an amount of 1.5 to 3g/L.
3. A metal surface cleaner according to claim 1 wherein the metal is stainless steel, an aluminium alloy or a titanium alloy, preferably an aluminium alloy.
4. The metal surface cleaning agent according to claim 1, wherein the metal is used as an anode, the inert metal is used as a cathode, the cleaning agent is used as an electrolyte, and a power source is applied between the metal and the inert technology to clean the metal of the anode.
5. The metal surface cleaning agent according to claim 4, wherein the power source is a DC power source and then a pulse power source, and the pulse is a millisecond pulse and then a microsecond pulse.
CN202210963879.4A 2022-08-11 2022-08-11 Metal surface cleaning agent Pending CN115233283A (en)

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