CN101724880A - Electrolyte, anodization method and anodized silicon-aluminum alloy - Google Patents

Electrolyte, anodization method and anodized silicon-aluminum alloy Download PDF

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CN101724880A
CN101724880A CN200810216925A CN200810216925A CN101724880A CN 101724880 A CN101724880 A CN 101724880A CN 200810216925 A CN200810216925 A CN 200810216925A CN 200810216925 A CN200810216925 A CN 200810216925A CN 101724880 A CN101724880 A CN 101724880A
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electrolytic solution
silumin
ion
equivalent
metaphosphate
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CN101724880B (en
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谢呈德
高乡明
涂俊凯
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Hangzhou Win Win Technology Co ltd
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BYD Co Ltd
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Abstract

The invention provides an electrolyte, an anodization method and an anodized silicon-aluminum alloy. The electrolyte contains equivalent silicate ions and equivalent metaphosphate ions, wherein the equivalent silicate ions refer to silicate ions converted from all ions and particles containing a silicon element based on equal silicon element content, and the quivalent metaphosphate ions refer to metaphosphate ions converted from all ions and particles containing a phosphor element based on equal phosphor element content; and the electrolyte refers to an alkaline hydrosol. By adopting the electrolyte, an anodization film with good hardness, wear resistance and corrosion resistance can be formed on the surface of the silicon-aluminum alloy.

Description

A kind of electrolytic solution, anode oxidation method and anodised silumin
Technical field
The present invention relates to a kind of electrolytic solution, especially a kind of anodic oxidation electrolyte of silumin, and the anodised silumin that uses this electrolytic solution to obtain.
Background technology
Silumin, especially the anodic oxidation of silumin (massfraction of Si element is not less than 1%) is difficult, reason is in the common anode oxidation process, Si in the alloy both had been insoluble to acid electrolyte, did not also react with electrolytic solution, residued in alloy surface after the anodic oxidation and formed " silicon ash ", make the oxide film surface blackening and stain occur, reduce homogeneity, compactness and the glossiness of oxide film, thereby make the performance of oxide film, reduce greatly as hardness, wear-resisting, corrosion-resistant etc.Silicone content is high more, and the anodic oxidation of alloy is difficult more, and the performance of the oxide film that obtains is poor more.
Summary of the invention
For solving the problem that silumin of the prior art is difficult to form hardness, wear-resisting, anode oxide film that erosion resistance is good, the present invention at first provides a kind of electrolytic solution, with this electrolytic solution silumin is carried out anodic oxidation, can form hardness, wear-resisting, oxide film that erosion resistance is good at alloy surface.
Two of purpose of the present invention provides the described electrolytic solution of a kind of use silumin is carried out anodised method.
Three of purpose of the present invention provides a kind of silumin anodic oxidation product that is obtained by above-mentioned anode oxidation method.
For achieving the above object, the present invention at first provides a kind of electrolytic solution, comprise equivalent silicate ion, equivalent metaphosphate ion, described equivalent silicate ion refers to contain in the electrolytic solution all ions of element silicon and particulate and equates that by silicon content the silicate ion that is converted to, described equivalent metaphosphate ion refer to that all ions of phosphorus element-containing in the electrolytic solution and particulate equate the metaphosphate ion that is converted to by phosphorus element content; Described electrolytic solution is alkaline water colloidal sol.
The present invention also provides a kind of silumin anodised method:
To be immersed in according in the electrolytic solution of the present invention through pretreated silumin, the control maximum voltage is no more than 360V and carries out anodic oxidation.
The present invention and then a kind of anodised silumin is provided adopts the method according to this invention preparation, its oxide thickness 10~20 μ m, and hardness 〉=HV400 is in the erosion resistance neutral salt spray continuously more than the 40h.
Beneficial effect of the present invention:
1. electrolytic solution raw material according to the present invention is easy to get, cheap, environmental friendliness.
2. anode oxidation method according to the present invention is simple to operate, need not special process.
3. all better according to hardness, wear resistance, erosion resistance, the sticking power of silumin anodic oxidation product oxide film of the present invention.
Embodiment
Silumin according to the present invention refers to that the massfraction of element silicon is not less than 1% silumin in the alloy.
Describe the present invention below in detail.
The specific embodiment of the present invention provides a kind of electrolytic solution, comprises equivalent silicate ion, equivalent metaphosphate ion, and all ions and particulate that described equivalent silicate ion refers to contain in the electrolytic solution element silicon (Si) (are SiO 3 2-Hydrolysate) equate the silicate ion (SiO that is converted to by Si content 3 2-), described equivalent metaphosphate ion refers to that all ions of phosphorus element-containing in the electrolytic solution (P) and particulate (are PO 3 -Hydrolysate) equate the metaphosphate ion (PO that is converted to by P content 3 -), described electrolytic solution is alkaline water colloidal sol.
Electrolytic solution is made into the alkali solution colloidal sol that contains above-mentioned equivalent silicate ion, equivalent metaphosphate ion can realizes the present invention, principle is the application of sol-gel method in electrochemical filming, and essence is to form even, fine and close oxide film by following 2 factors at alloy surface: lyosol is to Al 3+, H +, OH -The attached control of absorption-desorption Al 3+, H +, OH -Velocity of diffusion; The lyosol system also impels electric field distribution even.
Silicate ion SiO 3 2-Intense hydrolysis is alkalescence, forms the hydrolysate of multiple complexity such as poly silicate ion, silicic acid, multi-silicate micelle, makes solution be colloidal sol or gel, so simple silicate ion SiO 3 2-In solution, exist hardly.So the present invention has introduced above-mentioned SiO 3 2-Hydrolysate equate the notion of " the equivalent silicate ion " that be converted to by Si content.If SiO 3 2-It is acid that the PH of solution is, and then silica gel can become white precipitate.If SiO 3 2-Concentration makes hydrolyzed solution be gel too greatly, and then the anode oxide film of Sheng Chenging is inhomogeneous, and poor-performing can not be realized the present invention.So should control electrolytic solution is alkaline water colloidal sol.Alkalescence, two controlling factors of the water-sol can be controlled the concentration of equivalent silicate ion to realize the present invention.
Metaphosphoric acid radical PO 3 -A little less than the hydrolysis, its hydrolysis can form multiple complicated hydrolysates such as polymetaphosphate radical ion, polyphosphoric acid radical ion, and hydrolyzed solution is slightly acidic or neutrality.(the pH value 6~9 of the Trisodium trimetaphosphate aqueous solution of massfraction 1% (0.03mol/L) under the room temperature.) simple metaphosphoric acid radical PO 3 -In solution, exist hardly, so the present invention has introduced above-mentioned PO 3 -Hydrolysate equates the notion of " the equivalent metaphosphate ion " that be converted to by P content.PO 3 -(form with equivalent metaphosphate ion in solution exists) is a kind of buffer reagent commonly used, and effect in the present invention also is a buffer reagent.The contriver finds that equivalent metaphosphate ion is to realizing that the present invention is necessary.The content of equivalence metaphosphate ion is to guarantee that electrolytic solution is that the alkaline water colloidal sol that contains equivalent silicate ion and equivalent metaphosphate ion exceeds.That is to say, electrolytic solution is made into the alkaline water colloidal sol that comprises described equivalent silicate ion and described equivalent metaphosphate ion, promptly define the concentration of equivalent metaphosphate ion.
Described equivalent silicate ion is by soluble silicate, silicic acid (H 2SiO 3), orthosilicic acid (H 4SiO 4), silicon-dioxide (SiO 2) at least a providing, described equivalent metaphosphate ion is by at least a the providing in metaphosphoric acid, the solubility metaphosphate.If select soluble silicate for use, as water glass (Na 2SiO 3), potassium silicate (K 2SiO 3), get then that it is water-soluble in right amount, add at least a in metaphosphoric acid, the solubility metaphosphate then, be made into the alkaline water-sol and get final product; If select silicic acid (H for use 2SiO 3), orthosilicic acid (H 4SiO 4) or silicon-dioxide (SiO 2), then it should be dissolved in the aqueous solution of alkali earlier, as sodium hydroxide (NaOH), potassium hydroxide (KOH), ammoniacal liquor (NH 3H 2O) the aqueous solution makes silicic acid (H 2SiO 3), orthosilicic acid (H 4SiO 4) or silicon-dioxide (SiO 2) generate corresponding soluble silicate with alkali reaction, add at least a in metaphosphoric acid, the solubility metaphosphate (as Trisodium trimetaphosphate, Sodium hexametaphosphate 99) then, obtain alkaline water colloidal sol.
The concentration of described alkaline water colloidal sol intermediate ion is preferably descended train value:
Equivalence silicate ion concentration 0.04~0.2mol/L,
Equivalence metaphosphate ion concentration 0.02~0.2mol/L.
The hardness of the silumin anode oxide film that obtains like this, wear resistance, erosion resistance, sticking power are all better.
Described electrolytic solution can also contain alkaline buffer reagent, adds hardness and wear resistance that alkaline buffer reagent can improve the silumin anode oxide film.The alkalescence buffer reagent refers to that water-soluble back PH is the buffer reagent of alkalescence.Described alkaline buffer reagent preferred boric acid salt buffer reagent.Can be by in described electrolytic solution, adding the solubility borate, as borax (Na 2B 4O 710H 2O), or the borate buffer solution for preparing, make as the method for tetraborate buffered soln and contain the borate buffer reagent in the electrolytic solution.Preferred 0.005~the 0.03mol/L of the concentration of described borate buffer reagent in described electrolytic solution (, referring to that then solute in the tetraborate buffered soln is to the concentration of described electrolytic solution) if add the tetraborate buffered soln prepare.The contriver discovers, contains hardness and wear resistance that the borate buffer reagent can improve the silumin anode oxide film in the described electrolytic solution.But the collocation method of reference standard borate buffer solution, according to the concentration of above-mentioned preferred borate buffer reagent, the configuration borate buffer solution.The collocation method of standard borate buffer solution: take by weighing borax (Na 2B 4O 710H 2O) (3.80 ± 0.01) g (noting: can not dry by the fire) is dissolved in and boiled in advance in 15~30min and the rapid refrigerative distilled water, and is diluted to 1000ml.Put airtight preservation in the vinyon bottle.To prevent airborne CO when depositing 2Enter.
The pH value of described electrolytic solution can pass through exogenously added alkali according to circumstances, as NaOH, KOH, NH 3H 2O controls.The pH value of described electrolytic solution is 10~11 o'clock, and the slickness of gained oxide film is best, so preferred PH=10~11.
Described anodic oxidation electrolyte can also contain additive, and described additive is selected from least a in transistion metal compound that transition metal oxygen acid radical ion can be provided after water-soluble, solubility polyoxometallate, the solubility heteropoly compound.Describedly can provide the transistion metal compound of transition metal oxygen acid root to comprise transition metal oxide, transition metal complex, transition metal oxygen acid, transition metal oxysalt after water-soluble.The effect of described additive comprises: the performance such as wear resistance, hardness, erosion resistance, electrical insulating property of improving the silumin anode oxide film; Make the silumin anode oxide film have distinct colors.The example of described additive such as soluble tungstate salt, molybdate, vanadate, V 2O 5, MoO 3, WO 3, MnO 2, CrO 3The contriver studies have shown that: add tungsten compound, molybdenum compound or vanadium compound that one or more can provide the oxygen acid radical ion of tungsten, molybdenum or vanadium after water-soluble, as soluble tungstate salt, soluble molybdenum hydrochlorate or soluble vanadium hydrochlorate, can improve the wear resistance of oxide film.The addition of described additive is not more than 20g/ and rises electrolytic solution.In addition, the contriver finds, adds the tungsten compound that the oxygen acid radical ion of tungsten can be provided after water-soluble in electrolytic solution, as soluble tungstate salt, can improve the slickness of oxide film.
Described anodic oxidation electrolyte can also contain anion surfactant and/or amphoterics.The effect of described tensio-active agent comprises the aperture that reduces anode oxide film, improves the homogeneity of film.Preferred 1~the 5g/ of the addition of described tensio-active agent rises electrolytic solution.The example of described tensio-active agent such as Sodium dodecylbenzene sulfonate, sodium lauryl sulphate, disodium ethylene diamine tetraacetate.
A kind of silumin anode oxidation method:
To be immersed in according in the electrolytic solution of the present invention through pretreated silumin, the control maximum voltage is no more than 360V, and preferred maximum voltage is no more than 320V and carries out anodic oxidation.The preferred constant current oxidation of described anodic oxidation, more preferably pulse constant current oxidation.Also the may command maximum voltage is no more than 360V, and preferred maximum voltage is no more than 320V, adopts alternating-current to carry out anodic oxidation.When using alternating-current, the color of the oxide film that obtains meeting difference and direct current, other performances of oxide film such as hardness, wear resistance, erosion resistance etc. can be poorer slightly than pulse direct current, but still can realize the present invention.
According to general knowledge known in this field, the difference of hard anodizing technology and common anode oxidizing process is: hard anodizing need be controlled lower electrolyte temperature (generally being no more than 20 ℃).So adopt the anodised processing parameter of silumin according to the present invention, the control electrolyte temperature can carry out hard anodizing to silumin below 20 ℃.Dying not only to be used for the common anode oxidation process of silumin according to electrolytic solution of the present invention, also can be used for the hard anodizing technology of silumin.
Can be not less than 1% the well behaved oxide film of silumin surface formation at the massfraction of Si according to electrolytic solution of the present invention and anode oxidation method thereof, certainly also can be used for the common anode oxidation of the ordinary silicon aluminium alloy of Si massfraction lower (being not more than 1%), and hard anodizing technology.
A kind of anodised silumin, the method according to this invention preparation is characterized in that oxide thickness 10~20 μ m, hardness 〉=HV400 is in the erosion resistance neutral salt spray continuously more than the 40h.
In the silumin (Al-Si alloy), Si is main alloy element, and Si improves the flowability of alloy, reduces the thermo-cracking tendency, reduces and loosens, and improves resistance to air loss.This class alloy has good erosion resistance, medium intensity, hardness and medium machining property.Press Si content difference in the alloy, can be divided into different models, its performance is also different with purposes.Silumin has higher high temperature strength, good thermostability and wear resistance, is widely used in fields such as automobile, electronics, as parts such as the piston of motor car engine, cylinder sleeve, body, brake shoes, belt wheel, phone housing and inner member etc.Castability, mechanical behavior under high temperature, wear resisting property as the ZL108 type alloy of Si content 10~13% are all better, can be used to make internal combustion engine.The massfraction of Si generally surpasses 15% in the hypereutectic silumin.This class alloy is with the increase of Si content, and density reduces, and thermal expansivity reduces, and hardness, wear resistance and system stability improve, mainly as piston material.
Embodiment 1
At first AC1A silumin (Si element massfraction 1.2%) is carried out surface preparation, its step comprises degreasing, washing.Concrete technology is as follows:
Degreasing: the AD1A silumin is immersed carry out skimming treatment in the washing lotion (solvent is a water) of following composition:
Yellow soda ash 25g/L
Sodium phosphate 20g/L
Tripoly phosphate sodium STPP 5g/L
Sodium hydroxide 0.5g/L
Washing: with the surface of the AD1A silumin after deionized water rinsing skimming treatment 2min.
By the electrolytic solution under the following formulated room temperature, solvent is 1 premium on currency then:
Water glass (Na 2SiO 3) 0.12mol/L (15g/L)
Trisodium trimetaphosphate (NaPO 3) 30.013mol/L (4g/L)
Borax (Na 2B 4O 710H 2O) 0.013mol/L (5g/L)
Sodium wolframate (Na 2WO 42H 2O) 5g/ rises electrolytic solution
Disodium ethylene diamine tetraacetate (EDTA-2Na) 3g/ rises electrolytic solution
Water glass (Na 2SiO 3) the equivalent silicate ion in the electrolytic solution, Trisodium trimetaphosphate (NaPO be provided 3) 3Equivalent metaphosphate ion in the electrolytic solution is provided.15g water glass (Na 2SiO 3) (0.12mol) be dissolved in 1L water after, the amount of substance of the equivalent silicate ion in the solution (mol) equals Na 2SiO 3Middle SiO 3 2-Amount of substance, be 0.12mol.4g Trisodium trimetaphosphate (NaPO 3) 3(0.013mol) be dissolved in 1L water after, the amount of substance of the equivalent metaphosphate ion in the solution (mol) equals (NaPO 3) 3Middle PO 3 -Amount of substance, be 0.039mol.
Then carry out anodic oxidation: will put into anodizing tank through the AD1A silumin of degreasing, washing, and adopt the direct impulse pattern to carry out anodic oxidation.The negative electrode of oxidation trough is a stainless steel plate, and anode is the AD1A silumin, and conducting medium is above-mentioned electrolytic solution, 25 ℃ of tank liquor temperatures.Anodised other processing parameters are as follows:
Frequency 500HZ
Dutycycle 20%
Current density 5A/dm 2,
Pulse direct current constant current oxidation, voltage stop oxidation after being raised to 300V from 0, obtain even, fine and close, ganoid taupe oxide film.
Embodiment 2
Carry out the pre-treatment of surperficial degreasing, washing with reference to 1 pair of ADC7 silumin of embodiment (Si element massfraction 4.5~9.5%).
By the silumin anodic oxidation electrolyte under the following formulated room temperature, solvent is 1 premium on currency then:
Water glass (Na 2SiO 3) 0.12mol/L (15g/L)
Trisodium trimetaphosphate (NaPO 3) 30.033mol/L (10g/L)
Borax (Na 2B 4O 710H 2O) 0.010mol/L (4g/L)
Sodium orthomolybdate (Na 2MoO 42H 2O) 8g/ rises electrolytic solution
Disodium ethylene diamine tetraacetate (EDTA-2Na) 2g/ rises electrolytic solution
Carry out anodic oxidation with reference to 1 pair of ADC7 silumin of embodiment then, different is the prescription and the anode oxidation process parameter of electrolytic solution.The prescription of electrolytic solution as above, the anode oxidation process parameter different with embodiment 1 is as follows:
Frequency 300HZ
Dutycycle 25%
Current density 10A/dm 2,
Pulse direct current constant current oxidation, voltage stop oxidation after being raised to 320V from 0, obtain even, fine and close, ganoid brown oxide film.
Embodiment 3
Carry out the pre-treatment of surperficial degreasing, washing with reference to 1 pair of ADC12 silumin of embodiment (Si element massfraction 9.6~12%).
By the silumin anodic oxidation electrolyte under the following formulated room temperature, solvent is 1 premium on currency then:
Water glass (Na 2SiO 3) 0.082mol/L (10g/L)
Trisodium trimetaphosphate (NaPO 3) 30.020mol/L (6g/L)
Borax (Na 2B 4O 710H 2O) 0.026mol/L (10g/L)
Sodium wolframate (Na 2WO 42H 2O) 5g/ rises electrolytic solution
Sodium orthomolybdate (Na 2MoO 42H 2O) 10g/ rises electrolytic solution
Disodium ethylene diamine tetraacetate (EDTA-2Na) 1g/ rises electrolytic solution
Carry out anodic oxidation with reference to 1 pair of ADC12 silumin of embodiment then, different is the prescription and the anode oxidation process parameter of electrolytic solution.The prescription of electrolytic solution as above, the anode oxidation process parameter different with embodiment 1 is as follows:
Frequency 1000HZ
Dutycycle 35%
Current density 15A/dm 2,
Pulse direct current constant current oxidation, voltage stop oxidation after being raised to 280V from 0, obtain even, fine and close, ganoid taupe oxide film.
Embodiment 4
Carry out the pre-treatment of surperficial degreasing, washing with reference to 1 pair of AC8A silumin of embodiment (Si element massfraction 11~13%).
By the silumin anodic oxidation electrolyte under the following formulated room temperature, solvent is 1 premium on currency then:
Water glass (Na 2SiO 3) 0.16mol/L (20g/L)
Trisodium trimetaphosphate (NaPO 3) 30.039mol/L (12g/L)
Borax (Na 2B 4O 710H 2O) 0.013mol/L (5g/L)
Ammonium meta-vanadate (NH 4VO 3) 2g/ rises electrolytic solution
Sodium orthomolybdate (Na 2MoO 42H 2O) 5g/ rises electrolytic solution
Disodium ethylene diamine tetraacetate (EDTA-2Na) 4g/ rises electrolytic solution
Carry out anodic oxidation with reference to 1 pair of AC8A silumin of embodiment then, different is the prescription and the anode oxidation process parameter of electrolytic solution.The prescription of electrolytic solution as above, the anode oxidation process parameter different with embodiment 1 is as follows:
Frequency 800HZ
Dutycycle 15%
Current density 8A/dm 2,
Pulse direct current constant current oxidation, voltage stop oxidation after being raised to 250V from 0, obtain even, fine and close, ganoid taupe oxide film.
Embodiment 5
Carry out the pre-treatment of surperficial degreasing, washing with reference to 1 pair of AC8A silumin of embodiment.
By the silumin anodic oxidation electrolyte under the following formulated room temperature, solvent is 1 premium on currency then:
Water glass (Na 2SiO 3) 0.123mol/L (15g/L)
Trisodium trimetaphosphate (NaPO 3) 30.026mol/L (8g/L)
Borax (Na 2B 4O 710H 2O) 0.010mol/L (4g/L)
Ammonium meta-vanadate (NH 4VO 3) 15g/ rises electrolytic solution
Sodium wolframate (Na 2WO 42H 2O) 8g/ rises electrolytic solution
Disodium ethylene diamine tetraacetate (EDTA-2Na) 4g/ rises electrolytic solution
Carry out anodic oxidation with reference to 1 pair of AC8A silumin of embodiment then, different is the prescription and the anode oxidation process parameter of electrolytic solution.The prescription of electrolytic solution as above, the anode oxidation process parameter different with embodiment 1 is as follows:
Frequency 1500HZ
Dutycycle 30%
Current density 25A/dm 2,
Pulse direct current constant current oxidation, voltage stop oxidation after being raised to 300V from 0, obtain even, fine and close, ganoid black oxide film.
Embodiment 6
Carry out the pre-treatment of surperficial degreasing, washing with reference to 1 pair of AC1A silumin of embodiment.
By the silumin anodic oxidation electrolyte under the following formulated room temperature, solvent is 1 premium on currency then:
Water glass (Na 2SiO 3) 0.082mol/L (10g/L)
Trisodium trimetaphosphate (NaPO 3) 30.026mol/L (8g/L)
Carry out anodic oxidation with reference to 1 pair of AC8A silumin of embodiment then, different is the prescription and the anode oxidation process parameter of electrolytic solution.The prescription of electrolytic solution as above, the anode oxidation process parameter different with embodiment 1 is as follows:
Frequency 1500HZ
Dutycycle 30%,
Current density 20A/dm 2,
Setting pulse direct current constant current oxidation, voltage stop oxidation after being raised to 300V from 0.
Embodiment 7
With reference to the method for embodiment 6, difference is: water glass (Na 2SiO 3) 0.041mol/L (5g/L), contain the borax (Na of 0.013mol/L (5g/L) in the electrolytic solution 2B 4O 710H 2O), direct current density 20A/dm 2The constant current anodic oxidation.
Comparative Examples
The AC8A silumin does not carry out anodic oxidation treatment, directly tests correlated performance.
Each embodiment and Comparative Examples are carried out performance test.The reagent of using in the embodiment of the invention, raw material, testing method and standard, testing tool, test result are shown in following table 1~4.
Performance test:
1. corrosion resistance nature test
Silumin by GB GB6458-86 or the oxidation of ISO3768-1976 antianode carries out the erosion resistance test.
Test result: black splotch do not occur through the same silumin about 2min alloy surface after spraying salts solution of any surface-treated, and the silumin that the method that adopts the embodiment of the invention obtains sprayed salts solution after 48 hours, observed high silicon die casting aluminium sample surfaces without any variation in humidity cabinet.
2. sticking power test
To carry out the test of anode oxide film sticking power according to the method for GB ASTM-D3359 according to the silumin of the embodiment of the invention.The sticking power grade standard is as shown in table 3.
3. hardness test
To and not pass through the same silumin of any surface-treated according to the silumin of the embodiment of the invention according to the GB/T4340.1-1999 standard, (the prosperous great test set of Dongguan City company limited produces on the Vickers' hardness experimental machine, model 401MVA) test, pressure head 200 grams, 15 seconds loading times, test three points respectively, and calculate its arithmetical av.The results are shown in Table 4.
4. wearability test
To on RCA paper tape wear resistant instrument (the global detecting instrument in Dongguan company limited produces, model F350008), carry out wearability test according to the silumin of the embodiment of the invention.Load 175 grams, testing standard are the no sharp traces of 2000 circles.The result is as shown in table 4.
Table 1: embodiment of the invention agents useful for same and raw material
Chemical reagent/raw material Purity The source
Water glass (Na 2SiO 3) Analytical pure Guangdong brilliance chemistry company limited
Trisodium trimetaphosphate (NaPO 3) 3 Analytical pure Guangdong brilliance chemistry company limited
Borax (Na 2B 4O 7·10H 2O) Analytical pure Guangdong brilliance chemistry company limited
Sodium orthomolybdate (Na 2MoO 4·2H 2O) Analytical pure Guangdong chemical reagent factory
Sodium hydroxide (NaOH) Analytical pure Guangdong brilliance chemistry company limited
Ammonium meta-vanadate (NH 4VO 3) Analytical pure Guangdong chemical reagent factory
Chemical reagent/raw material Purity The source
Sodium wolframate (Na 2WO 4·2H 2O) Analytical pure Shanghai experiment reagent company limited
Disodium ethylene diamine tetraacetate (EDTA-2Na) Analytical pure Guangdong brilliance chemistry company limited
Table 2: used various testing method of the embodiment of the invention and instrument
The instrument title The place of production, model
The Vickers' hardness experimental machine The prosperous great test set of Dongguan City company limited, the 401MVA type
RCA paper tape wear resistant instrument Dongguan global detecting instrument company limited, the F350008 type
Salt-mist corrosion tester Southern Jiangsu, Wuxi testing installation company limited, the YWX/Q-250 type
Table 3 sticking power standard
Grade Implication
5B Scribing edge is smooth, at the edge of line and point of crossing place all do not have coating and come off
4B There is the peeling paint of small pieces at place, point of crossing in line, and the total area that comes off is less than 5%
3B Edge and place, point of crossing in line have the coating of small pieces to come off, and come off the total area between 5~15%
2B Edge and place, point of crossing in line have coating in blocks to come off, and come off the total area between 15~35%
1B Edge and place, point of crossing in line have coating in blocks to come off, and come off the total area between 35~65%
0B Edge and place, point of crossing in line have coating in blocks to come off, and the total area that comes off is greater than 65%
Table 4 anode oxide film The performance test results
Embodiment/Comparative Examples Film thickness Erosion resistance Sticking power Wear resistance (number of turns that cut occurs) Hardness
Example 1 14μm 48h 5B 2750 HV492
Embodiment/Comparative Examples Film thickness Erosion resistance Sticking power Wear resistance (number of turns that cut occurs) Hardness
Example 2 16μm 48h 5B 2865 HV486
Example 3 15μm 48h 5B 2806 HV493
Example 4 13μm 48h 5B 2706 HV490
Example 5 15μm 48h 5B 2930 HV500
Example 6 13μm 48h 5B 2200 HV428
Example 7 16μm 48h 5B 2688 HV475
Comparative Examples - 2min - Obvious cut promptly appears in 46 circles HV225
As can be seen from Table 4:
1. all better to erosion resistance, hardness, wear resistance that silumin carries out the oxide film that anodic oxidation obtains with the electrolytic solution (embodiment 6) that only contains equivalent silicate ion and equivalent metaphosphate ion.Electrolyte prescription, operating procedure are all simple.(evaluation of wear resistance: adopt the abrasion resistance test method of the embodiment of the invention, can think to reach 2000 circles, the oxide film wear resistance is better.)
2. comparing embodiment 1~5,7 and embodiment 6 can find out: with the electrolytic solution that contains equivalent silicate ion, equivalent metaphosphate ion and borate buffer reagent wear resistance and the hardness that silumin carries out the oxide film that anodic oxidation obtains is improved a lot.Wherein, the hardness of the product of embodiment 1~5,7 is carried out hard anodizing far above the silumin that adopts sulfuric acid electrolyte to element silicon massfraction 10~13% and is handled available 300~400HV hardness, both avoided hard anodizing to use sulfuric acid as of the pollution of electrolytic solution main component to environment, also need not to control low temperature in the anode oxidation process process, simplified technology.
3. the wear resistance of the oxide film of comparing embodiment 1~5 and embodiment 7 as can be seen: tungsten compound, molybdenum compound or vanadium compound that the oxygen acid radical ion of tungsten, molybdenum or vanadium can be provided after the electrolytic solution interpolation that contains equivalent silicate ion, equivalent metaphosphate ion and borate buffer reagent is water-soluble, as soluble tungstate salt, soluble molybdenum hydrochlorate or soluble vanadium hydrochlorate, can improve the wear resistance of oxide film.
In addition, the contriver finds, and is better to the slickness that silumin carries out the oxide film that anodic oxidation obtains with the electrolytic solution of interpolation soluble tungstate salt.
Hardness, wear resistance, erosion resistance, sticking power according to silumin anode oxide film of the present invention are all better, can be used for the above-mentioned performance requriements of silumin higher, especially hardness and the wear resistance product of having relatively high expectations, as mobile phone component (as shell, inner member, antenna etc.), automobile component, as the piston of engine, cylinder sleeve, body, brake shoes etc.

Claims (15)

1. electrolytic solution, comprise equivalent silicate ion, equivalent metaphosphate ion, described equivalent silicate ion refers to contain in the electrolytic solution all ions of element silicon and particulate and equates that by silicon content the silicate ion that is converted to, described equivalent metaphosphate ion refer to that all ions of phosphorus element-containing in the electrolytic solution and particulate equate the metaphosphate ion that is converted to by phosphorus element content; Described electrolytic solution is alkaline water colloidal sol.
2. according to the electrolytic solution of claim 1, described ionic concentration is as follows:
Equivalence silicate ion concentration 0.04~0.2mol/L,
Equivalence metaphosphate ion concentration 0.02~0.2mol/L,
Described electrolytic solution is alkaline water colloidal sol.
3. according to the electrolytic solution of claim 1, also contain alkaline buffer reagent.
4. according to the electrolytic solution of claim 1, also contain the borate buffer reagent.
5. according to the electrolytic solution of claim 3, the concentration of the described electrolytic solution of described borate buffer reagent mesoboric acid salt pair is 0.005~0.03mol/L.
6. according to the electrolytic solution of claim 1, PH=10~11.
7. according to the electrolytic solution of claim 1, also contain additive, described additive is selected from least a in transistion metal compound that transition metal oxygen acid radical ion can be provided after water-soluble, solubility polyoxometallate, the solubility heteropoly compound.
8. according to the electrolytic solution of claim 5, the addition of described additive is not more than 20g/ and rises electrolytic solution.
9. according to the electrolytic solution of claim 1, also contain anion surfactant and/or amphoterics.
10. according to the electrolytic solution of claim 7, the addition of described tensio-active agent is that 1~5g/ rises electrolytic solution.
11. silumin anode oxidation method:
To be immersed in any one electrolytic solution of claim 1~9 through pretreated silumin, the control maximum voltage is no more than 360V and carries out anodic oxidation.
12. silumin anode oxidation method:
To be immersed in any one electrolytic solution of claim 1~9 through pretreated silumin, the control maximum voltage is no more than 320V and carries out anodic oxidation.
13. an anodised silumin according to the preparation of any one method of claim 9~10, is characterized in that oxide thickness 10~20 μ m, hardness 〉=HV400 is in the corrosion-resistant neutral salt spray continuously more than the 40h.
14. mobile phone component adopt and make according to the anodised silumin of claim 13.
15. automobile component adopt and make according to the anodised silumin of claim 13.
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