JP2003119572A - Treatment liquid for surface control before phosphating metal, and surface controlling method - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a treatment liquid for surface control superior in temporal stability, which is used prior to forming the phosphated film, in order to efficiently form a phosphated film consisting of fine crystallites. SOLUTION: The treatment liquid for surface control prior to metal phosphating treatment is characterized by including one or more phosphate particles selected from phosphates containing one or more divalent metals or trivalent metals, and one or more orthophosphoric acids, polyphosphoric acids, or phosphates thereof, as an acceleration component. The phosphate particles preferably include those with particle diameters of 5 μm or less, and have a content of 0.001-30 g/L. The one or more divalent metals or trivalent metals are preferably selected among Zn, Fe, Mn, Ni, Co, Ca, and Al.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a phosphate film chemical conversion treatment applied to the surface of a steel material, a galvanized steel sheet, and a metal material such as aluminum and a magnesium alloy. The present invention also relates to a surface-conditioning treatment liquid and a surface-conditioning method which are used for shortening the time and making the crystals of the phosphate coating finer.

[0002]

2. Description of the Related Art Recently, metal surfaces have been used to improve corrosion resistance after coating in automobile phosphate treatment, and to reduce friction during pressing or extend press die life in phosphate treatment for plastic working. It is required to form fine and dense phosphate-coated crystals. Therefore, for the purpose of activating the metal surface in order to obtain fine and dense phosphate film crystals, and forming nuclei for precipitation of phosphate film crystals,
A surface conditioning step is adopted before the phosphate film chemical conversion treatment step. The general phosphate coating chemical conversion process which is carried out to obtain fine and dense phosphate coating crystals is illustrated below.

[0003] (1) Degreasing (2) Washing with water (multi-stage) (3) Surface adjustment (4) Phosphate film conversion treatment (5) Washing with water (multi-stage) (6) Washing with pure water.

The surface conditioning step is used to make the phosphate coated crystals fine and dense. Regarding the composition thereof, for example, US Pat.
It is known from No. 2349 and No. 2310239, and titanium, pyrophosphate ion, orthophosphate ion, sodium ion and the like are disclosed as main constituents contained in the surface conditioner. The surface conditioning composition is referred to as "Jernstead salt", and its aqueous solution contains titanium ions and titanium colloid.

The titanium colloid is adsorbed on the metal surface by immersing or spraying the degreased and washed metal in an aqueous solution of the surface conditioning composition. The adsorbed titanium colloid serves as a nucleus for precipitation of phosphate film crystals in the subsequent phosphate film chemical conversion treatment step, which makes it possible to accelerate the chemical conversion reaction and to make the phosphate film crystals finer and denser. All of the surface conditioning compositions currently used industrially utilize a Jernstead salt. However, when titanium colloid obtained from Jernstead salt is used in the surface conditioning step, there are various problems.

The first problem is the deterioration of the surface conditioning treatment liquid over time. When a conventional surface conditioning composition is used, it exhibits a remarkable effect on the fineness and densification of phosphate coating crystals immediately after the composition is made into an aqueous solution. However, after several days have passed since the solution was made into an aqueous solution, the titanium colloid aggregates to lose its effect regardless of whether or not the surface conditioning treatment liquid is used, and the obtained phosphate coating crystals become coarse. .

Therefore, in JP-A-63-76883, the average particle diameter of titanium colloid in the surface adjusting treatment solution is measured, and the surface adjusting treatment solution is prepared so that the average particle diameter becomes less than a certain value. A method has been proposed in which the surface conditioning effect is maintained and managed by continuously discarding and supplementing the discarded surface conditioning composition. However, although this method made it possible to quantitatively control the factors for the effect of the surface conditioning treatment liquid, it was necessary to discard the surface conditioning treatment liquid in order to maintain the effect. Further, in order to maintain the effect of the surface conditioning treatment liquid by this method at the same level as in the initial stage when the aqueous solution was prepared, it is necessary to discard a large amount of the surface conditioning treatment liquid. Therefore, there is also a problem with the wastewater treatment capacity of the factory that is actually used, and continuous disposal of the surface treatment liquid and total renewal are used together to maintain its effect.

A second problem is that the effect and life of the surface conditioning treatment liquid are greatly affected by the quality of water used when the bath is prepared. Usually, industrial water is used when the surface conditioning treatment liquid is set up. However, as is well known, industrial water contains cation components such as calcium and magnesium that are the basis of total hardness,
Its content varies depending on the source of the industrial water used. Here, it is known that the titanium colloid, which is the main component of the conventional surface conditioning treatment liquid, has an anionic charge in the aqueous solution and is dispersed without settling due to its electric repulsive force. There is. Therefore, when a large amount of cation components, calcium and magnesium, are present in industrial water, the titanium colloid is electrically neutralized by the cation component, loses its repulsive force and causes cohesive precipitation, thereby losing its effect.

Therefore, a method has been proposed in which a condensed phosphate such as pyrophosphate is added to the surface conditioning treatment liquid for the purpose of blocking the cation component and maintaining the stability of the titanium colloid. However, when a large amount of condensed phosphate is added to the surface conditioning treatment liquid, condensed phosphoric acid reacts with the surface of the steel sheet to form an inactive film, resulting in poor chemical conversion in the subsequent phosphate film chemical conversion treatment process. It has harmful effects. Further, in an area having an extremely high magnesium or calcium content, it is necessary to use pure water for the bath preparation and water supply of the surface conditioning treatment liquid, which is extremely economically disadvantageous. The third problem is restrictions on temperature and pH under the usage conditions.
Specifically, when the temperature is 35 ° C. or higher and the pH is in the range other than 8.0 to 9.5, the titanium colloid agglomerates and the surface adjusting effect cannot be exerted. Therefore, when using the conventional surface conditioning composition, it is necessary to use it at a predetermined temperature and pH range, and the surface conditioning composition is added to a degreasing agent or the like to clean and activate the metal surface. It was impossible to exert the effect of 1 with one liquid for a long time.

A fourth problem is a limit value for miniaturization of phosphate coating crystals obtained by the effect of the surface conditioning treatment liquid. The surface conditioning effect is obtained by the adsorption of titanium colloid on the metal surface to form nuclei for the precipitation of phosphate coating crystals. Therefore, the larger the number of titanium colloids adsorbed on the metal surface in the surface conditioning step, the finer and denser phosphate-coated crystals can be obtained.

For that purpose, it is easily conceivable to increase the number of titanium colloids in the surface conditioning treatment liquid, that is, increase the concentration of titanium colloids. However, when the concentration is increased, the frequency of collision between titanium colloids in the surface conditioning treatment liquid increases, and the collision causes coagulation and precipitation of titanium colloids. The upper limit of the concentration of titanium colloid currently used is 100 as titanium in the surface conditioning treatment liquid.
It is below ppm, and it has been impossible with the prior art to refine the phosphate coating crystal by increasing the titanium colloid concentration.

Therefore, in JP-A-56-156778 and JP-A-57-23066, an insoluble phosphate of a divalent or trivalent metal is added to the surface of the steel strip as a surface modifier other than the Jernstead salt. A surface conditioning method is disclosed in which the suspension containing is sprayed under pressure. However, this surface adjustment method is effective only when the suspension is sprayed on the object under pressure, so it is used for surface adjustment of the phosphate film chemical conversion treatment, which is usually performed by dipping and spraying. could not.

Further, Japanese Patent Publication No. 40-1095 discloses a surface conditioning method in which a galvanized steel sheet is immersed in a high-concentration divalent or trivalent metal insoluble phosphate suspension. However, the examples shown by this method are limited to galvanized steel sheets, and in order to obtain the surface conditioning effect, it was necessary to use a high concentration insoluble phosphate suspension of at least 30 g / L or more. . Therefore, despite the various problems of Jernstead salts being presented, to date, no new technology that can replace them has been presented.

[0014]

DISCLOSURE OF THE INVENTION The present invention has solved the above-mentioned problems of the prior art and, in the phosphate film chemical conversion treatment, promotes the chemical conversion reaction and shortens the time, and makes the obtained phosphate film crystals finer. It is an object of the present invention to provide a novel treatment liquid for surface adjustment and a method for surface adjustment, which are used for the purpose of achieving excellent stability over time.

[0015]

[Means for Solving the Problems] The present inventors have diligently studied means for solving the above problems, solving the problems in the conventional method, and further improving the quality of phosphate-coated crystals. The present inventors have completed a new surface conditioning treatment liquid and a surface conditioning method capable of achieving the above.

In the present invention, one or more kinds of phosphate particles selected from phosphates containing one or more kinds of divalent and / or trivalent metals, and one of orthophosphoric acid and polyphosphoric acid as a promoting component. It is a treatment liquid for surface conditioning before metal phosphate coating conversion treatment, characterized by containing at least one species.

The phosphate particles include those having a particle size of 5 μm or less, the concentration thereof is 0.001 to 30 g / L, and the divalent or trivalent metal is Zn, Fe, Mn,
It is preferably at least one selected from Ni, Co, Ca, and Al. Further, the total concentration of the accelerating component is preferably 1 to 2000 ppm.

Further, it is preferable that the aqueous solution contains an alkali metal salt, an ammonium salt or a mixture thereof. The alkali metal salt or ammonium salt is one of orthophosphate, metaphosphate, orthosilicate, metasilicate, carbonate, bicarbonate, nitrate, nitrite, sulfate, borate, and organic acid salt. At least one selected from the above, and the concentration thereof is 0.5 to 20 g / L
Is preferred.

The surface conditioning method before the metal phosphate coating conversion treatment of the present invention is characterized in that the metal surface is brought into contact with the surface conditioning treatment liquid.

Further, the surface conditioning treatment liquid of the present invention has a high p
Since the stability in the H range and the stability at high temperatures are extremely superior to the titanium colloids of the prior art, nonionic surfactants or anionic surfactants, or mixtures thereof, and alkali By adding a builder, it can be used also in a degreasing and surface conditioning treatment method that combines cleaning and activation of the metal surface.

An example of the phosphate chemical conversion coating treatment process in which the surface conditioning treatment liquid of the present invention is used in the degreasing and surface conditioning process is shown below. By using the surface conditioning treatment liquid of the present invention in the degreasing and surface conditioning step, it is possible to omit the water washing step during the degreasing surface conditioning, which was impossible in the prior art. Since the surface conditioning treatment liquid of the present invention can be used in a wide pH range and various alkali metal salts can be added, the step (1) may be performed depending on the surface contamination of the metal to be treated. Prior to the degreasing and surface conditioning step, the preliminary washing or preliminary degreasing step can be used.

[0022] (1) Degreasing and surface adjustment (2) Phosphate film conversion treatment (3) Washing with water (multi-stage) (4) Washing with pure water.

[0023]

BEST MODE FOR CARRYING OUT THE INVENTION The action of each component in the present invention will be described in detail. One or more kinds of phosphate particles selected from phosphates containing one or more kinds of divalent and / or trivalent metals (hereinafter, simply referred to as "divalent or trivalent metal phosphate particles") And the promoting component are essential components in the present invention. As described above, the object of the present invention is to provide a surface conditioning treatment liquid used for activating the metal surface prior to the phosphate treatment and forming nuclei for the precipitation of phosphate coating crystals. The present inventors have found that divalent or trivalent metal phosphate particles having a certain specific concentration and particle size are adsorbed on the surface of the metal to be treated in an aqueous solution containing a certain specific accelerating component, and the phosphorus They have found that they act as nuclei for the precipitation of acid salt film crystals and further increase the reaction rate of phosphate chemical conversion treatment.

Further, since the divalent or trivalent metal phosphate particles are components similar to the phosphate chemical conversion treatment bath and the phosphate chemical conversion treatment film, they are brought into the phosphate chemical conversion treatment bath. However, it also has the advantage that it does not adversely affect the chemical conversion treatment bath and that it does not adversely affect the performance of the phosphate chemical conversion coating even if it is incorporated into the phosphate coating as nuclei. Examples of the divalent or trivalent metal phosphate particles used in the present invention include the following examples.

Zn ₃ (PO ₄ ) ₂ , Zn ₂ Fe (PO ₄ ) ₂ , Zn ₂ Ni (PO ₄ ) ₂ , Ni
₃ (PO ₄ ) ₂ , Zn ₂ Mn (PO ₄ ) ₂ , Mn ₃ (PO ₄ ) ₂ , Mn ₂ Fe (PO ₄ ) ₂ , Ca ₃ (PO ₄ )
_{2, Zn 2 Ca (PO 4} ) 2, FePO 4, AlPO 4, CoPO 4, Co 3 (PO 4) 2 and its like hydrate.

It is known that the grain size of the phosphate coating crystals formed on the surface of the metal to be treated becomes finer as the number of crystals deposited per unit area in the initial stage of the reaction increases. This is because the growth of crystals in the phosphate coating is completed when adjacent crystals come into contact with each other and completely cover the metal surface.Therefore, the larger the number of crystals precipitated in the initial stage of the reaction, the smaller the distance between adjacent crystals. This is because minute crystals cover the metal surface in a short time. Therefore, in order to precipitate fine phosphate crystals in a short time, it is effective to add a large number of crystal nuclei before the phosphate chemical conversion treatment. It goes without saying that the smaller is, the more advantageous.

Further, in order to stably disperse the insoluble substance in the aqueous solution, it is desirable that the particle diameter of the divalent or trivalent metal phosphate particles used in the present invention is 5 μm or less. However, even if divalent or trivalent metal phosphate particles having a particle size of 5 μm or more are present in the surface conditioning treatment liquid of the present invention, they have no effect on the effect of the present invention. That is, the effect is exhibited only when the concentration of fine particles of 5 μm or less in the surface conditioning treatment liquid reaches a certain concentration.

Further, the divalent or trivalent metal phosphate particles used in the present invention not only serve as nuclei for the precipitation of phosphate crystals, but also have the effect of promoting the precipitation reaction. . That is, a part of the divalent or trivalent metal phosphate particles adsorbed on the metal surface in the surface conditioning treatment step is dissolved in the phosphate chemical conversion treatment bath, so that phosphoric acid is brought into close proximity to the metal surface. Since the main component of the salt crystals is supplied, the initial precipitation reaction of the phosphate crystals is significantly accelerated.

In order to serve as nuclei for the precipitation of the phosphate crystals and to accelerate the initial precipitation reaction of the phosphate crystals,
The phosphate particle concentration of the divalent or trivalent metal is preferably 0.001 to 30 g / L. This is because the concentration of divalent or trivalent metal phosphate particles is 0.001.
If it is less than g / L, the amount of divalent or trivalent metal phosphate particles adsorbed on the metal surface is too small to promote the initial precipitation reaction of the phosphate crystals, and the nuclei of the crystals are not promoted. The reaction is not promoted because the number of particles of the divalent or trivalent metal phosphate, which are Even if the phosphate particle concentration of the divalent or trivalent metal is higher than 30 g / L, the effect of further accelerating the phosphate chemical conversion reaction cannot be obtained, and thus it is economically disadvantageous. is there.

Next, the accelerating component that is essentially contained in the surface conditioning treatment liquid of the present invention will be described. As shown in the prior art, in the past, a method of spraying an insoluble phosphate of a divalent or trivalent metal under pressure to adjust the surface has been tried. However, in the past methods, it was necessary to spray an insoluble phosphate of a divalent or trivalent metal under pressure. The reason for spraying under pressure is that in order to exert the surface conditioning effect, it was necessary to hit an insoluble phosphate against the metal surface to cause a reaction, or to scratch the metal surface like shot peening. Further, in order to obtain the surface conditioning effect by the dipping treatment, it has been necessary to extremely increase the concentration of the insoluble phosphate of the divalent or trivalent metal in the conventional method.

The present inventors have found that the presence of any of the accelerating components of the present invention to be described later results in a low concentration of divalent or trivalent metal phosphate particles and a physical force on the metal surface. It has been found that the surface conditioning effect can be exhibited even in the dipping treatment without addition of. Therefore, in the present invention, it suffices to bring the treated material into contact with the surface conditioning treatment liquid,
The reaction mechanism is completely different from that of the prior art.

The accelerating component of the present invention enhances the dispersion stability of divalent or trivalent metal phosphate particles and promotes the adsorption of divalent or trivalent metal phosphate particles on the metal surface. Have a function to do. That is, the accelerating component is adsorbed on the surface of the divalent or trivalent metal phosphate particles, and due to the repulsive force and steric hindrance of the charge, the phosphoric acid of the divalent or trivalent metal in the surface conditioning treatment liquid is used. Prevents coagulation and sedimentation by preventing collision between salts. Further, since the accelerating component has the ability to adsorb to the metal surface due to its structure, it promotes the adsorption of divalent or trivalent metal phosphate particles to the metal surface, and the surface conditioning treatment liquid is treated with the metal to be treated. The surface conditioning effect can be obtained simply by contacting.

The concentration of the accelerating component is preferably 1-2000 ppm. If this concentration is less than 1 ppm, the surface conditioning effect will not be exhibited only by bringing the metal to be treated into contact with the surface conditioning treatment solution, and if it exceeds 2000 ppm, no further effect can be expected, and an excessive accelerating component will not be treated. It may be adsorbed on the metal surface and interfere with the phosphate conversion treatment.

In the present invention (1) above, one or more kinds selected from monosaccharides, polysaccharides and derivatives thereof are contained as a promoting component. Examples of the basic saccharides of the monosaccharides, polysaccharides, and derivatives thereof used in the present invention include fructose, tagatose, psicose, sucrose, erythrose, threose, ribose, arabinose, xylose, lyxose, allose, altrose, glucose, mannose. , Gulose, idose, galactose and talose.

Therefore, when a monosaccharide is used, the basic constituent saccharide itself is used, when a polysaccharide is used, a homopolysaccharide or a heteropolysaccharide of the basic constituent saccharide is used, and as a derivative thereof, a hydroxyl group of the basic constituent saccharide is used. NO ₂ , C
H ₃ , C ₂ H ₄ OH, CH ₂ CH (OH) CH ₃ , CH ₂ CO
A monosaccharide obtained by etherification with a substituent such as OH or the like, a homopolysaccharide or a heteropolysaccharide containing a monosaccharide substituted with the substituent in its structure can also be used, and several kinds of monosaccharides,
Polysaccharides and their derivatives may be used in combination.

When the saccharides are classified, they may be classified into monosaccharides, oligosaccharides, and polysaccharides depending on the degree of hydrolysis, but in the present invention, those that produce two or more monosaccharides by hydrolysis. A polysaccharide, a saccharide that is not hydrolyzed by itself, is a monosaccharide.

Since the use of the present invention is irrelevant to the biochemical reaction, the effect is not influenced by the configuration of the basic constituent sugars and the light-transmitting property. Any combination of (+,-) can be used. Further, there is no problem even if the sodium salt or ammonium salt of the monosaccharide, the polysaccharide, and the derivative thereof is used to increase the water solubility of the monosaccharide, the polysaccharide, and the derivative thereof. Further, when it is difficult to solubilize water with the above structure, it may be used after being dissolved in an organic solvent having compatibility with water in advance.

In the present invention of the above (2), as the accelerating component,
Orthophosphoric acid, polyphosphoric acid or organic phosphonic acid compounds 1
Contains more than one seed. Orthophosphoric acid is orthophosphoric acid, and as polyphosphoric acid, pyrophosphoric acid, triphosphoric acid, trimetaphosphoric acid, tetrametaphosphoric acid, hexametaphosphoric acid or their sodium salts and ammonium salts can be used. As the organic phosphonic acid compound, aminotrimethylenephosphonic acid, 1-hydroxyethylidene-1,1-diphosphonic acid, ethylenediaminetetramethylenephosphonic acid, diethylenetriaminepentamethylenephosphonic acid or sodium salt thereof can be used. Further, it is possible to use one kind of orthophosphoric acid, polyphosphoric acid or organic phosphonic acid compound or a combination of several kinds thereof.

In the present invention of the above (3), as a promoter, a water-soluble polymer compound comprising a vinyl acetate polymer or its derivative or a copolymer of vinyl acetate and a monomer copolymerizable with vinyl acetate and vinyl acetate is used. Contains one or more. As the vinyl acetate polymer or its derivative in the present invention, polyvinyl alcohol which is a saponified product of vinyl acetate polymer, cyanoethylated polyvinyl alcohol obtained by further cyanoethylating polyvinyl alcohol with acrylonitrile, and acetalizing polyvinyl alcohol with formalin. Formalized polyvinyl alcohol obtained, urethane-ized polyvinyl alcohol obtained by urethane-forming polyvinyl alcohol with urea,
Also, a water-soluble polymer compound obtained by introducing a carboxyl group, a sulfone group, an amide group or the like into polyvinyl alcohol can be used. Further, acrylic acid, crotonic acid, maleic anhydride or the like can be used as the monomer copolymerizable with vinyl acetate in the present invention.

The above-mentioned vinyl acetate polymer or its derivative or the copolymer of vinyl acetate and a monomer copolymerizable with vinyl acetate and vinyl acetate can sufficiently exhibit the effects of the present invention as long as they are water-soluble. . Therefore, the effect is not affected by the degree of polymerization and the rate of introduction of functional groups, and it is possible to use one kind or a combination of several kinds of the above-mentioned monomers or copolymers. .

Next, at least one or more selected from the monomer represented by the following chemical formula 1 or the α, β unsaturated carboxylic acid monomer, which is the promoting component of the present invention (4), and The effect of the polymer or copolymer obtained by polymerizing the monomer and 50% by weight or less of the copolymerizable monomer will be described.

[0042]

[Chemical 1]

As the monomer represented by the chemical formula 1, thimel acrylate, ethyl acrylate, propyl acrylate,
Butyl acrylate, pentyl acrylate, methyl methacrylate, ethyl methacrylate, propyl methacrylate,
Butyl methacrylate, pentyl methacrylate, hydroxymethyl acrylate, hydroxyethyl acrylate, hydroxypropyl acrylate, hydroxybutyl acrylate, hydroxypentyl acrylate, hydroxymethyl methacrylate, hydroxyethyl methacrylate, hydroxypropyl methacrylate, methacrylic acid Hydroxybutyl, hydroxypentyl methacrylate, etc. can be used.

As the α, β unsaturated carboxylic acid monomer, acrylic acid, methacrylic acid, maleic acid or the like can be used. Vinyl acetate, styrene, vinyl chloride, vinyl sulfonic acid and the like can be used as the monomer copolymerizable with the above monomer. Further, even if a polymer obtained by polymerizing one kind of the above-mentioned monomers is used, a copolymer obtained by polymerizing a combination of several kinds of the above-mentioned monomers is used. You can use it without any problem.

Further, the treatment liquid for surface conditioning of the present invention may contain an alkali metal salt, an ammonium salt or a mixture thereof. Examples of the alkali metal salt or ammonium salt include orthophosphate, metaphosphate, orthosilicate, metasilicate, carbonate, bicarbonate, nitrate,
There is no particular limitation as long as it is in the form of at least one salt selected from the group consisting of nitrite, sulfate, borate, and organic acid salt. Further, there is no problem even if two or more kinds of the alkali metal salts or ammonium salts are used in combination.

The alkali metal salt or ammonium salt used in the present invention generally conforms to the alkali builder used in industrial detergents. That is, the effect expected of an alkaline builder of an industrial cleaning agent, the softening property in water, and the cleaning action of an oil component further enhance the liquid stability of the surface conditioning treatment liquid used in the present invention, and exhibit the effect as a cleaning agent. Let them do it.

The concentration of the alkali metal salt or ammonium salt is preferably 0.5 to 20 g / L. If the concentration is less than 0.5 g / L, the water softening action and the cleaning action are not exhibited, and if it exceeds 20 g / L, no further effect can be expected and it is economically disadvantageous.

Unlike the conventional method, the treatment liquid for surface conditioning in the present invention can continue its effect in any use environment. That is, it has the following advantages as compared with the conventional method. (1) High temporal stability. (2)
Even if a hardness component such as Ca or Mg is mixed, the effect does not deteriorate. (3) It can be used at high temperatures. (4) Various alkali metal salts can be added. (5) High stability in a wide pH range.

Therefore, it can also be used as a degreasing and surface conditioning agent which could not maintain a stable quality in the conventional method. At that time, in order to enhance the degreasing and cleaning power in the surface conditioning step, known inorganic alkali builders other than the alkali metal salts or ammonium salts, organic builders, and surfactants may be added. In addition, a known chelating agent, condensed phosphate or the like may be added in order to cancel the influence of the cation component brought into the surface conditioning treatment liquid regardless of the degreasing and surface conditioning.

In the surface conditioning method of the present invention, it is sufficient to bring the surface conditioning treatment liquid into contact with the metal surface.
There is no limitation on the temperature of the surface conditioning treatment liquid. Furthermore, the surface conditioning method of the present invention can be applied to any metal material that is subjected to a phosphate treatment such as steel, galvanized steel sheet, aluminum or aluminum alloy, and magnesium alloy.

Further, with respect to the phosphate chemical conversion treatment method which is carried out after the surface conditioning treatment of the present invention, any method such as a dipping treatment method, a spray treatment method and an electrolytic treatment method can be applied. Regarding the phosphate film to be deposited, if it is a phosphate, zinc phosphate, manganese phosphate,
And zinc calcium phosphate are not limited.

[0052]

EXAMPLES Next, the effects of applying the treatment liquid for surface conditioning of the present invention will be described in detail using examples and comparative examples. However, as an example of the phosphate treatment, zinc phosphate treatment for a coating base is shown, and the use of the surface conditioning treatment liquid in the present invention is not limited at all.

(Sample Plate) Abbreviations and details of the sample plates used in Examples and Comparative Examples are shown below. SPC (cold rolled steel sheet: JIS-G-3141) EG (double-sided electrogalvanized steel sheet: coating weight 20 g /
m ² ) GA (double-sided alloyed hot-dip galvanized steel sheet: coating weight 4
5 g / m ² ) Zn-Ni (double-sided electrogalvanized nickel-plated steel sheet: plating basis weight 20 g / m ² ) Al (aluminum plate: JIS-5052) MP (magnesium alloy plate: JIS-H-4201).

(Treatment Step) Each test plate was treated in the following steps. Alkali degreasing → Washing → Surface conditioning → Zinc phosphate coating formation → Water washing → Deionized water washing. For alkaline degreasing, Fine Cleaner L4460 (registered trademark: manufactured by Nippon Parkerizing Co., Ltd.) was diluted to 2% with tap water and sprayed at 42 ° C. for 120 seconds in both Examples and Comparative Examples.

The surface conditioning treatment was carried out by immersing the object to be treated using the surface conditioning treatment liquids of Examples and Comparative Examples described later. For the formation of the zinc phosphate coating, Palbond L3020 (registered trademark: manufactured by Nippon Parkerizing Co., Ltd.) was diluted to 4.8% with tap water in both the Examples and Comparative Examples to accelerate the component concentration, total acidity, free acidity, and acceleration. The concentration of the agent is adjusted to the concentration generally used for zinc phosphate treatment for automobiles at present, and
It was used by dipping for 120 seconds at ℃. Both the water washing and the deionized water washing are spraying at room temperature for 30 seconds.

(Evaluation Method of Zinc Phosphate Coating) The zinc phosphate coating formed after the surface conditioning treatment was subjected to the following method.
Its appearance, coating weight (C.W), coating crystal size (C.W.).
S) and P ratio were measured. Appearance: The presence or absence of scaliness and unevenness of the zinc phosphate coating was evaluated by visual observation. ⊚: Uniform and good appearance, ◯: Partially uneven, Δ: Uneven and scaled,
×: There is a lot of scaling, and ×: No chemical conversion film.

Coating weight (CW): The weight of the test plate after forming the zinc phosphate coating (W1 (g)) was measured, and then zinc phosphate was used under the following stripping solution and stripping conditions. The coating was peeled off, the weight of the test plate was measured (W2 (g)), and the value was calculated by the following formula. Coating weight (g / m ² ) = (W1-W2) / (area). Stripping solution: 50% chromic acid aqueous solution for cold-rolled steel sheet, stripping condition: dipping at 75 ° C for 15 minutes, and stripping solution: 2% by weight ammonium dichromate + 28% ammonia water for galvanized steel sheet 49% by weight + pure 49% by weight, peeling conditions: Dipping at room temperature for 15 minutes. In the case of aluminum and magnesium alloys, P in the zinc phosphate coating was quantified with a fluorescent X-ray analyzer, and the amount of adhering the hopeite coating was calculated from the P content. Film crystal size (CS): Zinc phosphate film was scanned with a scanning electron microscope (SE).
M) was used to observe an image magnified 1500 times to investigate the crystal grain size. P ratio: Only for SPC steel sheets in both Examples and Comparative Examples, the X-ray intensity (P) of phosphophyllite crystals in the zinc phosphate coating and the X-ray intensity (H) of hovite were measured using an X-ray diffractometer. Then, the P ratio was calculated by the following formula. P ratio = P / (P + H).

Table 1 shows the composition of the surface conditioning treatment liquid used in the embodiment of claim 1 of the present invention. Table 2 shows the composition of each surface conditioning treatment liquid used in Comparative Examples. The monosaccharides, polysaccharides, and their derivatives used are commercially available products such as Daicel Chemical Industries, Ltd., Daiichi Kogyo Seiyaku Co., Ltd., Asahi Kasei Kogyo Co., Ltd., Dainippon Pharmaceutical Co., Ltd. It was selected based on the type, degree of polymerization, substituents and degree of substitution. Regarding the substituents, chemical formula 2 exemplifies glucose, which is one of the basic constituent sugars.

[0059]

[Chemical 2]

In the case of glucose, the three hydroxyl groups R ¹ , R ² and R ³ can be etherified. In this example, the kind of the substituent and the degree of substitution (basic constituent sugar 1 by the substituent 1
The effect was investigated by changing the number of substitution of hydroxyl groups per unit). In addition, sodium salts were used for monosaccharides, polysaccharides and their derivatives having low water solubility. The aging test was performed after preparing the surface conditioning treatment liquid and leaving it at room temperature for 10 days.

(Example 1) 0.5 mol heated to 50 ° C.
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite (Zn ₂ Fe) partially containing ferric phosphate.
It was _{(PO 4) 2 · 4H 2} O). Phosphophyllite 1
After adding 50 g of the monosaccharides, polysaccharides, and their derivatives shown in Table 1 previously diluted and dissolved in isopropyl alcohol and water to 10 wt% with respect to kg, about 1 with a ball mill using zirconia beads having a diameter of 0.5 mm. Crushed for hours.
After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 1 g / L, and the solution was used as a treatment liquid for surface adjustment. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device (LA-920:
As a result of measurement by HORIBA, Ltd., it was 0.5 μm.

(Example 2) 0.5 mol / heated to 50 ° C.
1 mol of iron (II) sulfate solution 1 L, 1 mol / L zinc sulfate solution 1
00mL and 1mol / L sodium hydrogen phosphate solution 1
00 mL was added alternately to form a precipitate. After heating the aqueous solution containing the precipitate at 90 ° C. for 1 hour to age the precipitated particles,
Gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite (Zn ₂ Fe (PO ₄ ) ₂ ) partially containing ferric phosphate.
・ 4H ₂ O). The monosaccharides, polysaccharides, and their derivatives shown in Table 1 were previously mixed with isopropyl alcohol and water at 10 wt%.
After adding 100 g of the phosphophyllite to 1 kg of the diluted and dissolved product, it was pulverized for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. After crushing, the concentration of phosphophyllite in the suspension was 1 with tap water.
It was adjusted to g / L and used as a surface adjustment treatment liquid. The average particle size of the fine particles in the adjusted suspension was 0.5 μm as a result of measurement with the laser diffraction / scattering type particle size distribution measuring device.

Example 3 0.5 mol / heated to 50 ° C.
1 mol of iron (II) sulfate solution 1 L, 1 mol / L zinc sulfate solution 1
00mL and 1mol / L sodium hydrogen phosphate solution 1
00 mL was added alternately to form a precipitate. After heating the aqueous solution containing the precipitate at 90 ° C. for 1 hour to age the precipitated particles,
Gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite (Zn ₂ Fe (PO ₄ ) ₂ ) partially containing ferric phosphate.
・ 4H ₂ O). To 1 kg of the phosphophyllite, 100 g of monosaccharides, polysaccharides and their derivatives shown in Table 1 which had been previously diluted and dissolved in water to 10 wt% were added, and then a ball mill using zirconia beads having a diameter of 0.5 mm was used. Crushed for about 1 hour. After pulverization, tap water was adjusted so that the concentration of phosphophyllite in the suspension was 1 g / L. As a result of measuring the average particle size of the fine particles in the suspension after adjustment with the laser diffraction / scattering type particle size distribution measuring device,
It was 0.5 μm. Further, 0.5 g / L of sodium nitrite reagent was added as an alkali salt to be used as a surface conditioning treatment liquid.

Example 4 0.5 mol / heated to 50 ° C.
1 mol of iron (II) sulfate solution 1 L, 1 mol / L zinc sulfate solution 1
00mL and 1mol / L sodium hydrogen phosphate solution 1
00 mL was added alternately to form a precipitate. After heating the aqueous solution containing the precipitate at 90 ° C. for 1 hour to age the precipitated particles,
Gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (PO ₄ ) ₂
・ 4H ₂ O]. 1 kg of monosaccharides, polysaccharides, and their derivatives shown in Table 1 previously diluted and dissolved in water to 10 wt%
On the other hand, after adding 50 g of the phosphophyllite,
It was crushed for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. After pulverization, tap water was adjusted so that the concentration of phosphophyllite in the suspension was 1 g / L. As a result of measuring the average particle size of the fine particles in the suspension after adjustment with the laser diffraction / scattering type particle size distribution measuring device,
It was 0.5 μm. Further, 0.5 g / L of magnesium sulfate heptahydrate reagent was added as an alkali salt to be used as a surface conditioning treatment liquid.

Example 5 0.5 mol / heated to 50 ° C.
1 mol of iron (II) sulfate solution 1 L, 1 mol / L zinc sulfate solution 1
00mL and 1mol / L sodium hydrogen phosphate solution 1
00 mL was added alternately to form a precipitate. After heating the aqueous solution containing the precipitate at 90 ° C. for 1 hour to age the precipitated particles,
Gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (PO ₄ ) ₂
・ 4H ₂ O]. 1 kg of monosaccharides, polysaccharides, and their derivatives shown in Table 1 previously diluted and dissolved in water to 10 wt%
On the other hand, after adding 50 g of the phosphophyllite,
It was crushed for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 1 g / L, and the solution was used as a treatment liquid for surface adjustment. The average particle size of the fine particles in the adjusted suspension was 0.5 μm as a result of measurement with the laser diffraction / scattering type particle size distribution measuring device.

Example 6 0.5 mol / L heated to 50 ° C.
1 mol / L zinc sulphate solution 10 per 1 L iron (II) sulfate solution
0 mL and 1 mol / L sodium monohydrogen phosphate solution 10
0 mL was added alternately to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (PO ₄ ) ₂
4H ₂ O]. 1 kg of the monosaccharides, polysaccharides, and their derivatives shown in Table 1 previously diluted and dissolved in water to 10 wt% was added to 1 kg of the phosphophyllite, and then a ball mill using zirconia beads having a diameter of 0.5 mm was used. Crushed for about 1 hour. After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 1 g / L, and the solution was used as a treatment liquid for surface adjustment. The average particle size of the fine particles in the adjusted suspension was 0.5 μm as a result of measurement with the laser diffraction / scattering type particle size distribution measuring device.

Example 7 Monosaccharides and polysaccharides shown in Table 1
1 kg of Zn ₃ (PO ₄ ) ₂ .4H ₂ O reagent was added to 1 kg of water and its derivative diluted to 10 wt% in water, and then ball mill using zirconia beads with a diameter of 0.5 mm for about 1 hour. Crushed. After crushing, suspend in tap water
_{Zn 3 (PO 4) 2 ·} 4H 2 O concentration was used as a treatment liquid for surface conditioning was adjusted to a 1 g / L. The average particle size of the fine particles in the adjusted suspension was measured by the laser diffraction / scattering type particle size distribution measuring device, and was found to be 0.6 μm.

Example 8 Zn ₃ (PO ₄₎ 2.4H ₂ O Reagent 1 kg
On the other hand, 10 g of a monosaccharide, a polysaccharide, and a derivative thereof shown in Table 1 which had been previously diluted and dissolved in water to 10 wt% were added, and then the mixture was pulverized for about 1 hour by a ball mill using zirconia beads having a diameter of 10 mm. Zn in suspension with tap water after crushing
_{3 (PO 4) 2 · 4H} 2 O concentration was adjusted to 1 g / L.
As a result of measuring the average particle size of the fine particles in the suspension after adjustment with the above-mentioned laser diffraction / scattering type particle size distribution measuring device, 1.2
was μm. Further, 5 g / L of sodium metasilicate reagent was added as an alkali salt to be used as a surface conditioning treatment liquid.

(Example 9) 0.1 mol / L heated to 50 ° C.
1 mol / L zinc nitrate solution 2 per 1 L calcium nitrate solution
00 mL was added, and 200 mL of a 1 mol / L sodium dihydrogen phosphate solution was further added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was schortite [Zn ₂ Ca (PO ₄ ) ₂ .2H ₂ O]. The monosaccharides, polysaccharides, and their derivatives shown in Table 1 were diluted and dissolved in water to 10 wt% with respect to 1 kg of the above-mentioned Scholtite.
After adding 0 g, it was ground for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. After crushing, taphol was used to adjust the concentration of schortite in the suspension to 10 g / L. The average particle size of the fine particles in the adjusted suspension was 0.4 μm as a result of measurement with the laser diffraction / scattering type particle size distribution measuring device. Further, a solution containing 1 g / L of a sodium carbonate reagent as an alkali salt was used as a surface conditioning treatment liquid.

(Example 10) 0.1 mol heated to 50 ° C
To 1 L of a calcium nitrate solution of / L, 200 mL of a 1 mol / L zinc nitrate solution was added, and further 200 mL of a 1 mol / L sodium monohydrogen phosphate solution was added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was schortite [Zn ₂ Ca (PO ₄ ) ₂ .2H ₂ O]. After adding 10 g of the monosaccharides, polysaccharides, and their derivatives shown in Table 1 previously diluted and dissolved in water to 10 wt% with respect to 1 kg of schortite, a ball mill using zirconia beads having a diameter of 0.5 mm for about 1 hour. Crushed. After the pulverization, the scholtite concentration in the suspension was adjusted to 5 g / L with tap water. The average particle size of the fine particles in the adjusted suspension was 0.4 μm as a result of measurement with the laser diffraction / scattering type particle size distribution measuring device. Furthermore, the third as an alkali salt
10 g / L of sodium phosphate reagent, commercially available polyoxyethylene nonylphenol ether 2 as a surfactant
What added g / L was used as a surface adjustment treatment liquid. In this example, the degreasing treatment was not performed, and the test piece on which the rust preventive oil had been adhered was directly subjected to the surface conditioning treatment also for cleaning.

(Comparative Example 1) A surface conditioning treatment was carried out under standard conditions of an aqueous solution of PREPAREN ZN (registered trademark: manufactured by Nippon Parkerizing Co., Ltd.) which is a conventional surface conditioning treatment liquid.

(Comparative Example 2) As shown in Table 2, 0.5 g of magnesium sulfate heptahydrate reagent as an alkali salt was added to an aqueous solution of preparene ZN which is a conventional surface conditioning treatment liquid.
What added L was used as a surface adjustment treatment liquid.

Comparative Example 3 0.5 mol / L heated to 50 ° C.
1L of iron (II) sulfate solution of 1 mol / L of zinc sulfate solution 1
00mL and 1mol / L sodium hydrogen phosphate solution 1
00 mL was added alternately to form a precipitate. After heating the aqueous solution containing the precipitate at 90 ° C. for 1 hour to age the precipitated particles,
Gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (PO ₄ ) ₂
・ 4H ₂ O]. The phosphophyllite was pulverized with a ball mill using zirconia beads having a diameter of 0.5 mm until the average particle size in the suspension measured by the laser diffraction / scattering particle size distribution analyzer was 0.5 μm.
After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 1 g / L, and the solution was used as a treatment liquid for surface adjustment.

Comparative Example 4 0.5 mol / heated to 50 ° C.
1 mol of iron (II) sulfate solution 1 L, 1 mol / L zinc sulfate solution 1
00mL and 1mol / L sodium hydrogen phosphate solution 1
00 mL was added alternately to form a precipitate. After heating the aqueous solution containing the precipitate at 90 ° C. for 1 hour to age the precipitated particles,
Gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (PO ₄ ) ₂
・ 4H ₂ O]. The phosphophyllite was ground in a mortar for about 2 minutes. After crushing, it was diluted with tap water, filtered through a 5 μm paper filter, and the filtrate was discarded. The obtained precipitate was dried at 80 ° C for 1 hour, and 1 kg of dried powder
On the other hand, 50 g of a monosaccharide, a polysaccharide, and a derivative thereof shown in Table 1 which had been diluted and dissolved in isopropyl alcohol and water to 10 wt% were added. The dry powder and high molecular weight monosaccharides, polysaccharides, and their derivatives have a dry powder concentration of 1 g /
It was adjusted to L by tap water and used as a surface adjusting treatment liquid. The average particle size of the fine particles in the adjusted suspension was measured by the above laser diffraction / scattering type particle size distribution measuring device, and was 6.5 μm.

Table 3 shows the coating characteristics of the chemical conversion coatings obtained by the zinc phosphate treatment using the surface conditioning treatment liquid in the examples. Table 4 shows the coating characteristics of the chemical conversion coating obtained in the zinc phosphate treatment using the surface conditioning treatment liquid in each comparative example.

From Tables 3 and 4, it is confirmed that the surface conditioning treatment liquid of the present invention has significantly improved stability over time, which was a drawback of the prior art. Comparative Example 3 and Example 1
And from Example 2, the effects of monosaccharides, polysaccharides, and their derivatives on the surface conditioning effect have been clarified. Further, in Comparative Example 3, immediately after being prepared as the surface conditioning treatment liquid, although it was inferior to Example 1, it had a surface conditioning effect equal to or higher than that of Comparative Example 1 which is a conventional technique.

However, in Comparative Example 3, it was extremely difficult to grind the divalent or trivalent metal phosphate, and 10
Precipitation of a divalent or trivalent metal phosphate salt occurred in the treatment solution after the passage of time. This is because in Comparative Example 3, the monosaccharide, the polysaccharide, and the derivative thereof are not added.
This is because re-aggregation of trivalent or trivalent metal phosphate has occurred. Further, even if the monosaccharide, the polysaccharide and its derivative, the kind of the alkali metal, and the treatment temperature were changed, the effect was not changed, and it was possible to obtain a fine and fine crystal which is equal to or more than the prior art.

Table 5 shows the composition of the surface conditioning treatment liquid used in the second embodiment of the present invention. In Comparative Examples 5 of Tables 5 and 2, orthophosphoric acid, polyphosphoric acid or organic phosphonic acid compounds are simply referred to as "phosphorus compounds". The phosphorus compounds used in Examples and Comparative Examples 5 in Table 5 were selected from reagents and commercially available products (for example, manufactured by Nippon Monsanto Industry Co., Ltd.) based on their structures. The effect of the present invention is not limited to the pH of the surface-treating treatment liquid, but when the pH of the phosphorus compound is extremely low, it is preliminarily hydroxylated to prevent dissolution of the divalent or trivalent metal phosphate. The pH of the phosphorus compound was adjusted to neutral with sodium. The aging test was performed after preparing the surface conditioning treatment liquid and leaving it at room temperature for 10 days.

Example 11 0.5 mo heated to 50 ° C.
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (P
O ₄₎ was ₂ · 4H ₂ O]. Phosphophyllite 1k
After adding 2 g of the phosphorus compound shown in Table 5 previously diluted and dissolved in water to 10 wt% with respect to g, it was pulverized for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 5 g / L. The average particle size of the fine particles in the adjusted suspension was 0.5 μm as a result of measurement with the laser diffraction / scattering type particle size distribution measuring device.
Further, 0.5 g / L of magnesium sulfate heptahydrate reagent was added as an alkali salt to be used as a surface conditioning treatment liquid.

Example 12 0.5 mo heated to 50 ° C.
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (P
O ₄₎ was ₂ · 4H ₂ O]. Phosphophyllite 1k
1 kg of a phosphorus compound shown in Table 5 previously diluted and dissolved in water to 10 wt% with respect to g was added, and then pulverized with a ball mill using zirconia beads having a diameter of 0.5 mm for about 1 hour. After pulverization, tap water was adjusted so that the concentration of phosphophyllite in the suspension was 1 g / L. The average particle size of the fine particles in the adjusted suspension was 0.5 μm as a result of measurement with the laser diffraction / scattering type particle size distribution measuring device.
1 g / sodium metasilicate reagent as an alkali salt
What added L was used as a surface adjustment treatment liquid.

(Example 13) 0.5 mo heated to 50 ° C.
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (P
O ₄₎ was ₂ · 4H ₂ O]. After adding 200 g of the above phosphophyllite to 1 kg of the phosphorus compound shown in Table 5 diluted and dissolved in water to 10 wt% in advance, it was pulverized for about 1 hour by a ball mill using zirconia beads having a diameter of 10 mm. After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 1 g / L, and the solution was used as a treatment liquid for surface adjustment. The average particle size of the fine particles in the adjusted suspension was measured by the above-mentioned laser diffraction / scattering type particle size distribution measuring device and found to be 1.7 μm.

[0082] (Example _{14) Zn 3 (PO 4)} 2 · 4H 2 O reagent 1k
After adding 100 g of the phosphorus compound shown in Table 5 previously diluted and dissolved in water to 10 wt%, the diameter of 0.5 m
Milled for about 1 hour with a ball mill using m zirconia beads. After milling, Zn ₃ (PO ₄₎ in suspension in tap water ₂ · 4H ₂ O
The concentration was adjusted to 5 g / L. The average particle diameter of the fine particles in the adjusted suspension was measured by the above-mentioned laser diffraction / scattering type particle size distribution measuring device, and was found to be 0.6 μm.
Further, 5 g / L of a sodium carbonate reagent was added as an alkali salt to be used as a surface conditioning treatment liquid.

(Example 15) 0.1 mo heated to 50 ° C
To 1 L of a 1 / L calcium nitrate solution, 200 mL of a 1 mol / L zinc nitrate solution was added, and further 200 mL of a 1 mol / L sodium monohydrogen phosphate solution was added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was schortite [Zn ₂ Ca (PO ₄ ) ₂ .2H ₂ O]. A phosphorus compound shown in Table 5 which was previously diluted and dissolved in water to 10 wt% 1
After adding 1 kg of scholtite to kg, it was crushed for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. After crushing, taphol was used to adjust the concentration of schortite in the suspension to 10 g / L. The average particle size of the fine particles in the adjusted suspension was 0.5 μm as a result of measurement with the laser diffraction / scattering type particle size distribution measuring device. Further, 10 g / L of a trisodium phosphate reagent was added as an alkali salt, and 2 g / L of a commercially available polyoxyethylene nonylphenol ether was added as a surfactant, which was used as a surface conditioning treatment liquid. In this example, the degreasing treatment was not performed, and the test piece on which the rust preventive oil had been adhered was directly subjected to the surface conditioning treatment also for cleaning.

Comparative Example 5 0.5 mol / heated to 50 ° C.
1 mol of iron (II) sulfate solution 1 L, 1 mol / L zinc sulfate solution 1
00mL and 1mol / L sodium hydrogen phosphate solution 1
00 mL was added alternately to form a precipitate. After heating the aqueous solution containing the precipitate at 90 ° C. for 1 hour to age the precipitated particles,
Gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (PO ₄ ) ₂
・ 4H ₂ O]. The phosphophyllite was ground in a mortar for about 2 minutes. After crushing, it was diluted with tap water, filtered through a 5 μm paper filter, and the filtrate was discarded. The obtained precipitate was dried at 80 ° C for 1 hour to obtain a powder. 100 g of the dry powder was added to 500 g of the phosphorus compound shown in Comparative Example 5 in Table 2 which had been previously diluted to 10 wt% with water, and the concentration of the dry powder was adjusted to 1 g / L with tap water. Used as a surface conditioning treatment liquid. The average particle size of the fine particles in the suspension after adjustment was 6.5 μm as a result of measurement by the above-mentioned laser diffraction / scattering type particle size distribution measuring device.

Table 6 shows the coating characteristics of the chemical conversion coatings obtained by the zinc phosphate treatment using the surface conditioning treatment liquid in the examples. Further, Comparative Example 5 in Table 4 shows coating characteristics of the chemical conversion coating obtained by the zinc phosphate treatment using the surface conditioning treatment liquid in Comparative Example 5.

From Tables 6 and 4, it is confirmed that the surface conditioning treatment liquid of the present invention has significantly improved stability over time, which was a drawback of the prior art. Comparative Example 3 and Example 1
The effect of orthophosphoric acid, polyphosphoric acid or organic phosphonic acid compound on the surface conditioning effect is clear from 3.

Immediately after preparation as a surface conditioning treatment liquid, Comparative Example 3 had a surface conditioning effect equal to or higher than that of Comparative Example 1 which is a conventional technique, although it was inferior to that of Example 11. However, in Comparative Example 3, it was extremely difficult to grind the divalent or trivalent metal phosphate, and the divalent or trivalent metal phosphate was not precipitated in the treatment solution after 10 days. It was happening. This is because in Comparative Example 3, orthophosphoric acid, polyphosphoric acid or an organic phosphonic acid compound was not added, so that re-aggregation of the divalent or trivalent metal phosphate occurred. Further, even if the orthophosphoric acid, the polyphosphoric acid or the organic phosphonic acid compound, the kind of the alkali metal, and the treatment temperature were changed, the effect was not changed, and it was possible to obtain a fine and fine crystal which is equal to or more than the prior art.

Table 7 shows the composition of the surface conditioning treatment liquid used in the embodiment of claim 3 of the present invention. In Comparative Examples 6 of Tables 7 and 2, a water-soluble polymer compound composed of a vinyl acetate polymer or its derivative or a copolymer of vinyl acetate and a monomer copolymerizable with vinyl acetate was simply referred to as “water-soluble polymer”. Polymer compound ". The vinyl acetate polymer or its derivative in the table was obtained by polymerizing vinyl acetate using a peroxide as an initiator and further imparting the functional groups shown in the examples by a saponification reaction, an acetalization reaction and the like. Further, a copolymer of vinyl acetate and a monomer copolymerizable with vinyl acetate was synthesized by a polymerization reaction of vinyl acetate and each monomer. The aging test was performed after preparing the surface conditioning treatment liquid and leaving it at room temperature for 10 days.

(Example 16) 0.5 mo heated to 50 ° C.
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (P
O ₄₎ was ₂ · 4H ₂ O]. Phosphophyllite 1k
10 g of the water-soluble polymer compound shown in Table 7 in advance with water.
0.5g after adding 2g diluted to wt%
It was crushed for about 1 hour by a ball mill using mm zirconia beads. After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 5 g / L. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was 0.5 μm.
Furthermore, 0.5% sodium metasilicate reagent as an alkali salt
What added g / L was used as a surface adjustment treatment liquid.

(Example 17) 0.5 mo heated to 50 ° C.
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (P
O ₄₎ was ₂ · 4H ₂ O]. After adding 100 g of the phosphophyllite to 500 g of the water-soluble polymer compound shown in Table 7, which had been previously diluted and dissolved in water to 10 wt%, and then pulverized with a ball mill using zirconia beads having a diameter of 0.5 mm for about 1 hour. did. After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 1 g / L, and the solution was used as a treatment liquid for surface adjustment. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was 0.5 μm.

[0091] For 1kg those diluted dissolved in 10 wt% in water in advance (Example 18) a water-soluble polymer compounds shown in Table _{7, Zn 3 (PO 4)} 2 · 4H 2 O reagent 50g After the addition, the diameter 0.
It was crushed for about 1 hour by a ball mill using 5 mm zirconia beads. After milling, Zn ₃ of suspension in tap water (PO _{4) 2} · ₄
The H ₂ O concentration was adjusted to 1 g / L. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was 0.5 μm. Further, 0.5 g / L of magnesium sulfate heptahydrate reagent was added as an alkali salt to be used as a surface conditioning treatment liquid.

Example 19 0.1 mo heated to 50 ° C.
To 1 L of a 1 / L calcium nitrate solution, 200 mL of a 1 mol / L zinc nitrate solution was added, and further 200 mL of a 1 mol / L sodium monohydrogen phosphate solution was added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was schortite [Zn ₂ Ca (PO ₄ ) ₂ .2H ₂ O]. To 1 kg of the water-soluble polymer compound shown in Table 7 previously diluted and dissolved in water to 10 wt%, 500 g of scholtite was added, and then pulverized for about 1 hour by a ball mill using zirconia beads having a diameter of 10 mm. After the pulverization, the scholtite concentration in the suspension was adjusted to 5 g / L with tap water. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was found to be 1.6 μm. Furthermore, 5 g of sodium carbonate reagent as an alkali salt
What added / L was used as a surface adjustment treatment liquid.

(Example 20) 0.1 mo heated to 50 ° C
To 1 L of a 1 / L calcium nitrate solution, 200 mL of a 1 mol / L zinc nitrate solution was added, and further 200 mL of a 1 mol / L sodium monohydrogen phosphate solution was added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was schortite [Zn ₂ Ca (PO ₄ ) ₂ .2H ₂ O]. 10 g of the water-soluble polymer compound shown in Table 7 previously diluted and dissolved in water to 10 wt% was added to 1 kg of schortite, and the mixture was pulverized for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. After the pulverization, the scholtite concentration in the suspension was adjusted to 30 g / L with tap water.
The average particle size of the fine particles in the adjusted suspension is determined by laser diffraction /
As a result of measurement with a scattering type particle size distribution measuring device, it was 0.3 μm. Further, 10 g / L of a trisodium phosphate reagent was added as an alkali salt, and 2 g / L of a commercially available polyoxyethylene nonylphenol ether was added as a surfactant, which was used as a surface conditioning treatment liquid. In this example, the degreasing treatment was not performed, and the test piece with the rust-preventing oil still attached was directly subjected to the surface conditioning treatment which also serves as cleaning.

Comparative Example 6 0.5 mol / heated to 50 ° C.
1 mol of iron (II) sulfate solution 1 L, 1 mol / L zinc sulfate solution 1
00m and 1mol / L sodium monohydrogen phosphate solution 10
0 mL was added alternately to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (PO ₄ ) ₂
4H ₂ O]. The phosphophyllite was ground in a mortar for about 2 minutes. After crushing, it was diluted with tap water, filtered through a 5 μm paper filter, and the filtrate was discarded. The obtained precipitate was dried at 80 ° C for 1 hour to obtain a powder. The water-soluble polymer compound shown in Comparative Example 6 in Table 2 was diluted and dissolved in water to 10 wt% to 500 g, and 100 parts of the dry powder was used.
After adding g, it was adjusted with tap water so that the concentration of the dry powder would be 1 g / L, and used as a treatment liquid for surface adjustment. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was 6.5 μm.

Table 8 shows the coating properties of the chemical conversion coatings obtained by the zinc phosphate treatment using the surface conditioning treatment liquid in the examples. In addition, Comparative Example 6 in Table 4 shows the film characteristics of the chemical conversion treatment film obtained by the zinc phosphate treatment using the surface conditioning treatment liquid in Comparative Example 6.

From Tables 8 and 4, it is confirmed that the surface conditioning treatment liquid of the present invention has significantly improved stability over time, which was a drawback of the prior art. Comparative Example 3 and Example 1
From 7 it is clear that the effect of the water-soluble polymer compound consisting of a vinyl acetate polymer or its derivative or a copolymer of vinyl acetate and a monomer copolymerizable with vinyl acetate on the surface conditioning effect. Further, in Comparative Example 3, immediately after being prepared as the surface conditioning treatment liquid, although it was inferior to Example 16, it had a surface conditioning effect equal to or higher than that of Comparative Example 1 which is a conventional technique.

However, in Comparative Example 3, it was extremely difficult to grind the divalent or trivalent metal phosphate, and 10
Precipitation of a divalent or trivalent metal phosphate salt occurred in the treatment solution after the passage of time. This is because in Comparative Example 3, a water-soluble polymer compound composed of a vinyl acetate polymer or its derivative or a copolymer of vinyl acetate and a monomer copolymerizable with vinyl acetate and a vinyl acetate was not added, and thus the divalent polymer was used. Another reason is that re-aggregation of trivalent metal phosphate occurred. Further, the effect is obtained even if the water-soluble polymer compound consisting of a vinyl acetate polymer or its derivative or a copolymer of vinyl acetate and a monomer copolymerizable with vinyl acetate, a kind of alkali metal, and a treatment temperature are changed. As a result, it was possible to obtain a fine and fine crystal having a size equal to or higher than that of the conventional technique.

Table 9 shows the composition of the surface conditioning treatment liquid used in the embodiment of claim 4 of the present invention. Polymers or copolymers were obtained by polymerizing the monomers of Comparative Example 7 in Tables 9 and 2 with ammonium persulfate as a catalyst. Further, with respect to a monomer having a difficulty in water solubility, it was polymerized after emulsification using a commercially available surfactant. In addition to the effect of the present invention,
There is no limitation on H, but when the pH of the polymer or copolymer is extremely low, the polymer or copolymer is preliminarily treated with sodium hydroxide in order to prevent dissolution of the divalent or trivalent metal phosphate. Was adjusted to neutral pH. The aging test was performed after preparing the surface conditioning treatment liquid and leaving it at room temperature for 10 days.

(Example 21) 0.5 mo heated to 50 ° C.
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (Pn
O ₄₎ was ₂ · 4H ₂ O]. Phosphophyllite 1k
1 g of the polymer or copolymer shown in Table 9 in advance with water.
After adding 1 g of a diluted solution of 0 wt%, the diameter was adjusted to 0.
It was crushed for about 1 hour by a ball mill using 5 mm zirconia beads. After crushing, the phosphophyllite concentration in the suspension was adjusted to 10 g / L with tap water. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was 0.5 μm. Furthermore, sodium nitrite reagent as an alkali salt was added to 0.1.
The solution added with 5 g / L was used as a treatment liquid for surface conditioning.

(Example 22) 0.5 mo heated to 50 ° C
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (P
O ₄₎ was ₂ · 4H ₂ O]. 100 g of the phosphophyllite was added to 500 g of the polymer or copolymer shown in Table 9 which had been previously diluted and dissolved in water to 10 wt%, and then the ball mill using zirconia beads having a diameter of 0.5 mm for about 1 hour. Crushed. After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 1 g / L, and the solution was used as a treatment liquid for surface adjustment. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was 0.5 μm.

(Example 23) 0.5 mo heated to 50 ° C.
To 1 L of a 1 / L iron (II) sulfate solution, 100 mL of a 1 mol / L zinc sulfate solution and 100 mL of a 1 mol / L sodium monohydrogen phosphate solution were alternately added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (P
O ₄₎ was ₂ · 4H ₂ O]. After adding 25 g of the above phosphophyllite to 1 kg of the polymer or copolymer shown in Table 9 previously diluted and dissolved in water to 10 wt%, it is about 1 hour in a ball mill using zirconia beads having a diameter of 0.5 mm. Crushed. After pulverization, tap water was used to adjust the concentration of phosphophyllite in the suspension to 0.5 g / L. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device and found to be 0.5 μm.
It was m. Furthermore, magnesium sulfate 7 as an alkali salt
The hydrate reagent added at 0.5 g / L was used as a surface conditioning treatment liquid.

Example 24 0.1 mo heated to 50 ° C.
To 1 L of a 1 / L calcium nitrate solution, 200 mL of a 1 mol / L zinc nitrate solution was added, and further 200 mL of a 1 mol / L sodium monohydrogen phosphate solution was added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was schortite [Zn ₂ Ca (PO ₄ ) ₂ .2H ₂ O]. To 1 kg of schortite, 1.5 g of the polymer or copolymer shown in Table 9 previously diluted and dissolved in water to 10 wt% was added, and then pulverized with a ball mill using zirconia beads having a diameter of 0.5 mm for about 1 hour. did. After crushing, taphol was used to adjust the concentration of schortite in the suspension to 10 g / L. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device and found to be 0.6 μm.
It was m. Further, a solution containing 1 g / L of a sodium carbonate reagent as an alkali salt was used as a surface conditioning treatment liquid.

(Example 25) 0.1 mo heated to 50 ° C
To 1 L of a 1 / L calcium nitrate solution, 200 mL of a 1 mol / L zinc nitrate solution was added, and further 200 mL of a 1 mol / L sodium monohydrogen phosphate solution was added to form a precipitate. The aqueous solution containing the precipitate was heated at 90 ° C. for 1 hour to age the precipitated particles, and then gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was schortite [Zn ₂ Ca (PO ₄ ) ₂ .2H ₂ O]. 20 g of a polymer or copolymer shown in Table 9 previously diluted and dissolved in water to 10 wt% was added to 1 kg of schortite, and the mixture was pulverized for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. After the pulverization, the scholtite concentration in the suspension was adjusted to 5 g / L with tap water.
The average particle size of the fine particles in the adjusted suspension is determined by laser diffraction /
As a result of measurement with a scattering type particle size distribution measuring device, it was 0.6 μm. Further, 10 g / L of a trisodium phosphate reagent was added as an alkali salt to be used as a surface conditioning treatment liquid.

Example 26 After adding 1 kg of Zn ₃ (PO ₄ ) ₂ .4H ₂ O reagent to 1 kg of the polymer or copolymer shown in Table 9 previously diluted and dissolved in water to 10 wt%, Diameter 1
It was crushed for about 1 hour with a ball mill using 0 mm zirconia beads. After milling, Zn ₃ of suspension in tap water (PO _{4) 2} · ₄
The H ₂ O concentration was adjusted to 1 g / L. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device and found to be 1.2 μm. Furthermore, as an alkali salt, 5 g of sodium metasilicate reagent /
L, commercially available polyoxyethylene nonylphenol ether 2 g / L as a surfactant was used as a surface conditioning treatment liquid. In this example, the degreasing process was not performed, and the test piece with the rust-preventive oil still attached was directly
A surface conditioning treatment that also serves as cleaning was performed.

[0105] (Example _{27) Zn 3 (PO 4)} 2 · 4H 2 O reagent 1k
1 g of the polymer or copolymer shown in Table 9 in advance with water.
After adding 50 g of a solution that was diluted and dissolved to 0 wt%, it was pulverized for about 1 hour by a ball mill using zirconia beads having a diameter of 0.5 mm. Zn ₃ (PO ₄ ) in suspension with tap water after grinding
_It was adjusted to a concentration of 2.4H ₂ O of 1 g / L and used as a surface conditioning treatment liquid. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was 0.5 μm.

Comparative Example 7 0.5 mol / heated to 50 ° C.
1 mol of iron (II) sulfate solution 1 L, 1 mol / L zinc sulfate solution 1
00mL and 1mol / L sodium hydrogen phosphate solution 1
00 mL was added alternately to form a precipitate. After heating the aqueous solution containing the precipitate at 90 ° C. for 1 hour to age the precipitated particles,
Gradient washing was repeated 10 times. The precipitate obtained by filtration was dried and analyzed by X-ray diffraction. As a result, the precipitate was found to contain phosphophyllite [Zn ₂ Fe (PO ₄ ) ₂
・ 4H ₂ O]. The phosphophyllite was ground in a mortar for about 2 minutes. After crushing, it was diluted with tap water, filtered through a 5 μm paper filter, and the filtrate was discarded. The obtained precipitate was dried at 80 ° C for 1 hour, and 1 kg of dried powder
On the other hand, 100 g of the polymer or copolymer shown in Comparative Example 7 in Table 2 was previously diluted and dissolved in water to 10 wt% and added. A mixture of the dry powder and the polymer or copolymer was adjusted with tap water so that the concentration of the dry powder was 1 g / L, and the mixture was used as a surface conditioning treatment liquid. The average particle size of the fine particles in the adjusted suspension was measured by a laser diffraction / scattering type particle size distribution measuring device, and was 6.5 μm.

Table 10 shows the coating characteristics of the chemical conversion coating obtained by the zinc phosphate treatment using the surface conditioning treatment liquid in the examples. In addition, Comparative Example 7 in Table 4 shows the film properties of the chemical conversion treatment film obtained in Comparative Example 7.

From Tables 10 and 4, it is confirmed that the surface conditioning treatment liquid of the present invention has significantly improved stability over time, which was a drawback of the prior art. From Comparative Example 3 and Examples 22 and 27, the effect of the polymer or copolymer on the surface conditioning effect is clear.

Immediately after preparation as the surface conditioning treatment liquid in Comparative Example 3, it had a surface conditioning effect equivalent to or better than that of Comparative Example 1 which is a conventional technique, though inferior to Example 21. However, in Comparative Example 3, it was extremely difficult to grind the divalent or trivalent metal phosphate, and the precipitation of the divalent or trivalent metal phosphate was observed in the treatment solution after 10 days. It was happening. This is because the polymer or copolymer was not added in Comparative Example 3, so that re-aggregation of the divalent or trivalent metal phosphate occurred. Furthermore, even if the type of polymer or copolymer, the type of alkali metal, and the treatment temperature were changed, the effect did not change, and it was possible to obtain finer and finer crystals than the prior art.

[0110]

[Table 1]

[0111]

[Table 2]

[0112]

[Table 3]

[0113]

[Table 4]

[0114]

[Table 5]

[0115]

[Table 6]

[0116]

[Table 7]

[0117]

[Table 8]

[0118]

[Table 9]

[0119]

[Table 10]

[0120]

As described above, the surface conditioning treatment liquid of the present invention markedly improves the stability over time which is a drawback of the titanium colloid of the prior art, and phosphate coating crystals which were impossible with the prior art. It is possible to further miniaturize the size. Therefore, the technique using the surface conditioning treatment liquid of the present invention is economically advantageous as compared with the conventional technique, and it is possible to provide the performance equal to or higher than that of the conventional technique.

   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Kensuke Shimoda             1-151-1 Nihonbashi, Chuo-ku, Tokyo Japan             Within Parkerizing Co., Ltd. (72) Inventor Hirokatsu Sakauchi             1-151-1 Nihonbashi, Chuo-ku, Tokyo Japan             Within Parkerizing Co., Ltd. F-term (reference) 4K026 AA01 AA02 AA07 AA09 AA12                       CA16 CA18 CA23 CA27 CA32                       CA33 CA38 EA10 EA15

Claims (12)

[Claims] 1. Particles of one or more kinds of phosphates selected from phosphates containing one or more kinds of divalent and / or trivalent metals, and orthophosphoric acid or polyphosphoric acid or phosphorus thereof as a promoting component. A treatment liquid for surface conditioning before metal phosphate coating conversion treatment, which comprises one or more acid salts. 2. The surface conditioning treatment liquid according to claim 1, wherein the accelerating component has an ability to be adsorbed on the surface of the phosphate particles. 3. The surface conditioning treatment liquid according to claim 1, wherein the accelerating component has the ability to be adsorbed on the surface of the metal to be treated. 4. The surface conditioning treatment liquid according to any one of claims 1 to 3, wherein the phosphate particles do not aggregate and settle. 5. The phosphate particles include those having a particle size of 5 μm or less, the concentration thereof is 0.001 to 30 g / L, and one or more kinds of divalent and / or trivalent metals are Zn, F
A treatment liquid for surface conditioning before metal phosphate coating conversion treatment according to any one of claims 1 to 4, which is selected from e, Mn, Ni, Co, Ca, and Al. 6. The total concentration of the accelerating component is 1 to 2000 p.
The surface conditioning treatment liquid before the metal phosphate coating conversion treatment according to any one of claims 1 to 5, which is pm. 7. A treatment liquid for surface conditioning before metal phosphate conversion treatment according to any one of claims 1 to 6, which further contains an alkali metal salt, an ammonium salt or a mixture thereof. . 8. An alkali metal salt or ammonium salt is orthophosphate, metaphosphate, orthosilicate, metasilicate, carbonate, bicarbonate, nitrate, nitrite, sulfate,
Before metal phosphate coating conversion treatment according to claim 7, which is at least one selected from borate and organic acid salt, and the concentration thereof is 0.5 to 20 g / L. Treatment liquid for surface conditioning. 9. Phosphorus metal comprising one or more phosphate particles selected from phosphates containing one or more divalent and / or trivalent metals and a promoting component. A surface conditioning treatment liquid before acid salt film conversion treatment, wherein the accelerating component has the ability to be adsorbed on the surface of the phosphate particles and the metal surface to be treated. And a treatment liquid for surface conditioning. 10. The surface conditioning treatment liquid according to claim 9, wherein the phosphate particles do not aggregate and settle. 11. A metal characterized by contacting the metal surface with the treatment liquid for surface conditioning according to any one of claims 1 to 10 before forming a phosphate conversion coating on the metal surface. Method of surface preparation before phosphate coating conversion treatment of. 12. When forming a phosphate chemical conversion coating on a metal surface, the metal surface is previously activated by a nonionic surfactant or anionic surfactant, or both of them are used to activate and clean the metal surface. A surface conditioning method before metal phosphate coating conversion treatment, which comprises bringing the mixture into contact with the surface conditioning treatment solution according to claim 1 containing an alkali builder.