JP4419968B2 - Electrolytic phosphate chemical treatment method and warm or hot forging method - Google Patents

Description

  The present invention provides a treatment bath for forming a film containing “phosphate crystals and metal” on a metal surface by electrolytic treatment, a method thereof, and a plastic working for heating an object to be processed at a temperature higher than a warm forging using the same. It relates to the lubrication process.

  Japanese Patent Application Laid-Open No. 2000-234200 (Patent Document 1) is a basic patent application relating to the electrolytic phosphate chemical treatment of the present inventor application. The feature is that the treatment bath does not contain metal ions other than the film-forming component in principle (0.4 g / L or less). Also, the composition of the treatment bath is 6-140 g / L for nitrate ions, 0.5-60 g / L for phosphate and phosphate ions, ions that form complexes with phosphate ions and dissolve in the treatment bath (such as zinc) However, it is characterized by 0.5 to 70 g / L, and metal ions deposited by reducing dissolved ions are 0 to 40 g / L.

Patent Document 1 Example 1 at a coating base in Example 3 and Example 4, when a current of 1A / dm ² or more current (Get workpiece 1 pc with 2 dm ^2), the electrolysis voltage is 9.6V The above is 17.7 V or more in terms of cathode treatment.

Japanese Patent Application Laid-Open No. 2002-322593 (Patent Document 2) is a patent application relating to electrolytic phosphate chemical conversion, also filed by the present inventor. This invention is characterized in that Patent Document 1 does not include an external reaction hindering substance (that is, a metal ion other than a film forming component) into the phosphate chemical treatment bath, whereas it is out of the reaction system. It controls the production of incoming interfering substance ions (N ₂ O ₄ gas, excess Fe ions).

  In Patent Document 2, the qualitative composition dissolved in the treatment bath is the same as Patent Document 1. In all the treatment bath compositions of the examples, the reduced and precipitated metal ions are in the range of 4.7 to 7.3 g / L and do not exceed 10 g / L. All the examples are electrolyzed at 8 V or higher.

  Japanese Patent Application Laid-Open No. 2004-52085 (Patent Document 3) is a patent relating to the electrolytic phosphate chemical treatment, also filed by the present inventor. This patent is characterized in that the rinse water after the phosphate chemical conversion treatment is electrodialyzed and the concentrated portion is returned to the treatment bath again. In this patent, knowledge about the electrolysis of the treatment bath components is obtained.

FIG. 3 of this patent document 3 shows that electrolysis of an electrodialysis bath containing an electrolytic treatment bath component can be seen in two forms. That is, electrodialysis with an applied voltage of 6 V or less indicates ion migration of only the solute component, but with 6 V or more, it is accompanied by electrolysis of water as a solvent. And in the electrolysis of 6V or more, the possibility of producing | generating sludge with the decomposition | disassembly of water is pointed out.
However, the display of FIG. 3 shows that 10 layers of electrolytic cells are stacked, and two electrolytic systems exist at a boundary of 0.6 V per electrolytic cell.

  That is, Patent Document 3 shows that the electrolytic phosphate chemical treatment is composed of two electrolytic treatment systems with respect to a change in voltage. FIG. 3 shows that the current (X axis) -voltage (Y axis) of the low electrolysis voltage system has a gentler gradient than that of the high electrolysis voltage system, and the electrolysis efficiency is good.

  That is, the electrolytic treatment at a low voltage suppresses the decomposition of water as a solvent and moves the solute component preferentially, thereby increasing the film formation efficiency.

  On the other hand, there is a processing technique called warm or hot forging in which a metal material is heated to 200 ° C. or higher and then plastically processed. This processing is employed in many metal materials such as steel, aluminum and its alloys, magnesium and its alloys.

  Japanese Laid-Open Patent Publication No. 6-1994 (Patent Document 4) relates to a lubrication treatment for cold and warm forging of a steel material. Among them, as a problem of the prior art, warm forging is performed by heating a forged product at 400 to 1000 ° C., but no suitable lubricant and its processing method are found.

  In cold forging, a method of forming a lubricating film by forming a phosphate conversion coating on a material to be forged and immersing it in an organic fatty acid salt (such as sodium stearate) bath has been established as a lubricating treatment. That is, a method for lubricating a forged material using a phosphate chemical coating has been established.

  On the other hand, in the conventional warm forging, a lubrication treatment is not performed in which a phosphate chemical conversion film is formed on a material to be forged and a film using a lubricant is formed thereon. This is because, in the temperature range of warm forging (about 400 to 1000 ° C.), since the phosphate chemical film formed by the conventional electroless method cannot secure adhesion with the base metal, the lubricating film is destroyed, This is because it does not function as a lubrication treatment. The role of the lubrication treatment is to interpose a lubricant between the mold and the material to be forged so that the mold and the material to be forged are not in direct contact with each other. However, it is difficult to ensure such a function unless the adhesiveness of the phosphate chemical film is secured at the temperature of warm forging.

  Therefore, in the conventional warm forging, the forged product is heated to about 250 to 300 ° C. and immediately after that, it is immersed in a liquid in which a solid lubricant such as graphite is dispersed, or a liquid containing graphite powder is sprayed. As a result, a graphite film is formed on the surface of the forged object, and subsequently, the forged object is heated to about 800 ° C., followed by a (warm forging) press. At that time, a lubricant is separately sprayed on the mold surface for mold lubrication. In addition, a method of simply applying the lubricant to the mold is performed without applying the lubricant to the forged object.

  However, in the processing method in which only the lubricant is applied to the forged material, the lubricant is only physically attached to the material to be forged, and is not attached with a chemical reaction with the material to be forged. When the die and the forged material are rubbed or rubbed strongly in the processed part of the material to be forged during pressing, the lubricant in the same part is easily removed and seizure occurs in that part. A problem occurs.

In Patent Document 4, as a countermeasure, a forged material is immersed in a solution composed of a water-soluble inorganic salt (K ₂ SO ₄ , Na ₂ B ₄ O ₄ , etc.) and molybdenum disulfide and / or graphite (graphite). The lubricating material is uniformly applied to the surface of the forged material and then dried to form a lubricating film composed of an inorganic salt and molybdenum disulfide and / or graphite (graphite) on the surface of the forged material. Furthermore, it is necessary to wash the forged material with hydrofluoric acid nitric acid during the process for forming the lubricating film. This pickling is performed in order to form a strong film on the surface. It is described that the lubricating film formed in this way exhibits a lubricating function for warm forging. However,
In the above description, the film is not formed by reacting on the surface of the material to be forged, but merely forming the film by physically attaching the solid content in the treatment bath to the chemically active surface.

  In addition, Patent Document 1 by the present inventor describes an invention relating to a phosphate chemical conversion film which is a base film formed on various forged materials. However, Patent Document 1 discloses a phosphate conversion coating composed of only a “phosphate + metal” coating with improved coating corrosion resistance applied to a coating base and a phosphate applied to a cold forging base. It only shows an example of formation. Further, there is no description or suggestion about applying the “phosphate + metal” film for hot forging or thermal forging lubrication.

  That is, the basic element of the electrolytic phosphate chemical treatment technique disclosed in Patent Document 1 is that the treatment bath does not substantially contain metal ions that do not become film components (400 ppm or less). And the form of a film | membrane contains the metal which does not become a phosphate (Claim 36, Example 1, 4 and 5), and the case where the metal which does not become a phosphate is contained (Claim 8, Example 2). It shows that there is.

  When a metal that does not become a phosphate is included, the film is composed of “phosphate + metal”. The metal contained in the film is a metal that has been reduced and deposited as a cation in the solution. And the film | membrane comprised from "phosphate + metal" has shown that a coating corrosion resistance is improved, when it employ | adopts for a coating ground treatment. The metal deposition makes it clear that the metal ions dissolved in the solution are reduced and deposited. It also indicates that it is necessary for the treatment bath not to contain metal ions (for example, sodium ions) that do not become film components in order to reduce and deposit the metal. This also shows that a film composed of “phosphate + metal” is impossible from an electroless treatment bath containing metal ions that do not become film components. It shows that such a difference in the undercoat causes a difference in the corrosion resistance of the coating.

  Moreover, in patent document 1, the Example (Example 2) used for cold forging is shown. And it is shown that the treatment bath composition and the film composition are significantly different between the cold forging example and the coating example. It shows that metal components other than phosphate are included for the coating base, but there are few metal components other than phosphate for the cold forging base.

  Table 1 shows a comparison of treatment methods, applications, treatment bath compositions, and film compositions in Examples and Comparative Examples of Patent Document 1.

  From the above comparison, the following can be confirmed.

  i. The film for cold forging is a film that does not contain a metal component (Ni) that does not become a phosphate.

  ii. The coating corrosion resistance is better for a film containing a metal component (Ni) that does not become a phosphate.

  That is, a film that does not contain a metal component that does not become a phosphate is good for cold forging (at a low temperature) lubrication treatment, but it is better that a metal component is included for coating corrosion resistance. This difference corresponds to the fact that the function of the phosphate chemical conversion coating is different between the coating undercoat and the cold forging lubrication.

  Next, the reason why the conventional phosphate chemical conversion coating film not containing Ni has been used for the cold forging lubrication process will be clarified. The cold forging lubrication function is the temperature range of cold forging (150 to 250 ° C). When the mold and the forged material (steel) come into contact with each other and the forged material changes plastically, the surface of the forged material is covered. The lubricant film (undercoat: phosphate + lubricant (sodium stearate, etc.)) is melted and fluidized to prevent direct contact between the material to be forged and the mold. is there. Therefore, the performance (item) required for the undercoat is: a. Chemical properties capable of holding the lubricant uniformly: ensuring chemical affinity with the lubricant, b. It is two points of fluidizing corresponding to a deformation | transformation of a to-be-forged material in the temperature range (150-250 degreeC) of a cold forging process. Said a is ensured by being the conventional phosphate conversion film "it does not contain the metal which reduced and deposited." And said b is ensured because the phosphate membrane | film | coat to form does not contain Ni.

In the film formed by the electroless treatment method, the treatment bath is limited in order to ensure the performances a and b described above. That is, it is achieved by suppressing the “reduced metal deposited by reduction” (generally Ni) in the treatment bath to 0.5 g / L or less. The conventional electroless-type cold forging phosphate chemical conversion coating is a coating that basically does not contain Ni or does not act, and satisfies the above a and b in the cold forging temperature region. Further, in the electroless system, it is basically impossible to deposit “metal that is reduced and deposited”. Therefore, in the electroless treatment method, since the electrolytic reaction voltage is equal to or lower than the decomposition voltage of water, it is not possible to form a thick film (for example, an adhesion mass of 5 g / m ² or more) suitable for forging containing Ni.

  On the other hand, the film formed by the electrolytic treatment method can deposit “metal that is reduced and deposited”. That is, a metal Ni having a high melting point (melting point: 1453 ° C.) may or may not be included in a form that is chemically reacted to the forged material. However, when a large amount of “metal that is reduced and deposited”, for example, Ni, is contained, the phosphate chemical conversion film does not satisfy the performance required for the steel materials cold forging of a and b. Therefore, such a coating does not apply to cold forging.

  In the examples in Table 1, the examples (Examples 1, 4 and 5) having improved coating corrosion resistance all contain a large amount of metal Ni. This indicates that the coating base film is preferably a film that contains a large amount of metal Ni that precipitates as the charge changes, and is strongly bonded to the base metal.

  Phenomena and evaluations related to coating corrosion resistance are performed in an environment of normal atmospheric pressure and room temperature. The peeling and deterioration of the coating contributed by the undercoat are reduced when the phosphate conversion coating is not chemically strongly bonded to the metal material. The strength of the bond between the metal material and the phosphate conversion coating increases in relation to the magnitude of the activation energy related to the coating formation reaction. The precipitation of the “reduced metal deposited” is accompanied by a change in charge. In contrast, “precipitation of phosphate crystals” is formed by a reaction that does not involve a change in the charge of the metal ions. The activation energies of the two reaction systems are different, and the precipitation reaction of “metal that is reduced and deposited” is larger. This corresponds to the fact that the film containing a large amount of Ni, which is a “metal that is reduced and deposited”, is strong to the base metal in the formation of the phosphate conversion film. And the results in Table 1 prove it.

  In the lubrication treatment related to cold forging, it is not advantageous that the adhesion between the phosphate chemical film and the base metal is large. The lubrication treatment requires that the surface be accompanied by fluidity in accordance with the plastic change of the material metal. Lubricity is the function of preventing the metal (press mold) and metal (raw material) from coming into direct contact. The film firmly bonded to the base metal tends to be plastically changed by being integrated with the base metal material. Therefore, fluidity will be impaired and lubricity will fall.

  The above-mentioned idea of the lubrication treatment in cold forging can be applied to warm forging. That is, it is desired that the phosphate chemical conversion film that requires lubricity used for warm forging is not integrated with the metal material at the plastic working temperature and pressure region, and has fluidity. That is, it is desired that the adhesion with the base metal is lowered in the temperature and pressure range of warm forging.

  Therefore, in the temperature range of cold forging (150 to 250 ° C.), a film that basically does not contain “metal that is reduced and deposited” is appropriate. However, with respect to maintaining the lubricity in the warm forging process in which the to-be-forged material is heated and then plastically processed, it is possible to use a film containing “a metal that is reduced and precipitates”.

  From the above, the phosphate chemical film formed by the electrolytic phosphate chemical treatment including the deposited metal does not have lubricity in the temperature range (150 to 250 ° C.) of cold forging. Although patent document 1 has shown about the film | membrane applied to a cold forging process, the possibility to a warm forging or a heat forging process is not described or suggested at all.

JP 2000-234200 A Japanese Patent Laid-Open No. 2002-322593 JP 2004-52085 A Japanese Patent Laid-Open No. 6-1994

The main purpose of the present invention is to improve the level of electrolytic phosphate chemical treatment technology.
(I) That is, an efficient control method of the electrolytic treatment technique is clarified and the reaction efficiency is improved.
(Ii) From that, practically more efficient electrolytic phosphate chemical treatment technology than before has been put into practical use and the scope of application can be expanded. That is, application to warm forging or heat forging lubrication.

First, “Clarify efficient control method of electrolytic treatment technology and improve reaction efficiency” will be explained.
The inventor classifies the phosphating baths into “processing baths that form a main film of phosphate” and “processing baths that form a metal + phosphate film”. This idea is explained by the present inventor in Patent Document 1.
The “treatment bath that forms the main film of phosphate” is composed mainly of phosphoric acid and “zinc, iron, or manganese, which is a metal that can be dissolved by dissolving phosphoric acid and dissociating phosphoric acid”. It is a solution containing “a metal nitrate as a film component” incidentally.
“Processing bath for forming a metal + phosphate film” includes “phosphoric acid” and “zinc, which is a metal that can be dissolved by dissolving phosphoric acid and dissociating phosphoric acid,” and “coating components. It is a treatment bath composed of a solution in which the metal nitrate is dissolved.
The former treatment bath is a general one in the conventional electroless treatment. The latter treatment bath is a treatment bath specific to electrolytic treatment. The subject of the present invention is the latter.

  “To clarify the efficient control method of the electrolytic treatment technique and improve the reaction efficiency” means that a film is formed by applying a large current at the lowest possible voltage. That is, a film is formed with a small amount of electric energy.

  In addition, “to broaden the application range, that is, to apply to warm forging lubrication” means that this technology is applied to warm forging or thermal forging lubrication that has not been applied in the past. is there.

  Another problem to be solved by the present invention is to improve the level of the lubrication process in the forging process in which the material to be forged is heated from room temperature to 200 ° C. or higher. The specific method is to form a lubrication film on the surface of the forged material that can withstand heating of 200 ° C. or higher (that is, the lubricating film does not desorb from the forged material even at a predetermined heating temperature) and lubricate. Is to do the processing. Such a lubrication treatment is performed on the mold and the forged material at a temperature that is “supported with the base metal material and can hold the lubricant” and “supported uniformly on the base film and heated. It is composed of a lubricant layer (film) that exhibits a lubricating function.

  The specific method of such a lubrication process varies depending on individual metal materials. This is because each material has different physical and chemical properties. However, the concept of the above-described lubrication treatment (formation of a lubricating film composed of a heat-resistant undercoat and a lubricating layer) is common regardless of the material.

  Lubricants are conventionally used in warm forging. Considering such a situation, the point of the problem to be solved by the present invention is to form a heat-resistant undercoat on various forged materials.

  Warm forging is most applied to steel materials. Therefore, the steel material will be described below as an example. When applied to steel materials, the object of the present invention is to provide a good lubrication treatment in a warm forging region of about 400 ° C. or higher, and “phosphate + metal” on the surface of the material to be forged at 400 ° C. or higher. It is achieved by uniformly forming a phosphate chemical conversion film composed of the following, and forming a lubricating film made of a lubricant having good lubricating performance at 400 ° C. or higher.

  As described above, the problem to be solved by the present invention is that a lubricant film is formed by forming a strong heat-resistant film (chemical conversion film) chemically bonded to the surface of the material to be forged and carrying a lubricant thereon. Is applied to the warm forging lubrication process.

Increasing the electrolytic reaction efficiency means reducing the electric resistance of the electrolytic treatment reaction system and flowing a large amount of current at a low voltage.
The current and ion flow in the electrolytic treatment will be described with reference to FIG. It is assumed that there is no electrical resistance between the DC power supply and the electrode / object to be processed.
In the above electrolytic treatment system, resistance is generated by (i) conversion on the electrode surface (electrode and treatment bath): conversion from current to ion transfer, (ii) stability of solution and ions in the treatment bath And (iii) conversion on the surface of the object to be processed: conversion from solution (ion) to solid (film): film formation.

  The above three points will be described.

(I) Conversion on the electrode surface: Regarding conversion from current to ion migration It is necessary that the current easily migrates from the electrode to dissolved ions. And it is desired that the ions to be mainly moved are film forming components. The film formed in the present invention is a “phosphate film containing a metal”. Therefore, the electrode material is the same material as the main component of the treatment bath, and a material that is deposited from the treatment bath to form a film is desirable. That is, it is desirable to use a metal as a film component as an electrode. Since the metal used as the film component is nitrate and contained in the treatment bath, the electrode material is a nitrate metal contained in the treatment bath.
In the electrolytic phosphate chemical treatment, not all of the current related to the electrode is consumed for dissolution. This is different from electroplating. In the electrolytic phosphate chemical treatment, a separate treatment bath is replenished in a form (metal ions) in which the same metal component as the electrode material is dissolved. Therefore, the applied current is divided into “dissolution of the electrode material” and “participating directly in the movement of the treatment bath components and reacting the component ions”.
To increase the electrolytic reaction efficiency is to increase the ratio to the portion “directly involved in the movement of the treatment bath components and react with component ions” and to control the reaction. Use of the same metal as the nitrate metal added to the treatment bath as the electrode material is effective for the above-described action.
However, in electroplating, such metal ions are not replenished as chemicals. Thus, all applied current is spent on dissolving the electrode material.

(Ii) Solution stability and ion migration in the treatment bath The main anion components of the treatment bath of the present invention are only phosphate ions and nitrate ions. If phosphate ions and nitrate ions are compared with the solubility of metal ions, nitrate ions> phosphate ions. Therefore, a solution containing a large amount of nitrate ions is advantageous in terms of solubility.
In the present invention, the state of the treatment bath of nitrate ion> phosphate ion is shown in a ratio in which metal ion from nitrate is 10 g / L and phosphoric acid and phosphate ion are 1/2 or less. . This clearly indicates the concentration of nitrate ions and the ratio of nitrate ions / phosphate ions. The treatment bath shows that the concentration of nitrate ions is a certain level (at least about 20 g / L) or more, and is about 4 times the concentration of phosphate ions.

(Iii) Conversion on the surface of the object to be processed: Conversion from solution (ion) to solid (film): film formation The deposited film components are “metal” and “phosphate”.
“Metal” is reduced and precipitated from the state in which nitrate is dissolved. If the nitrate component (nitrate ion + metal ion) is small, the dissolved ion concentration is lowered, and therefore the current efficiency is lowered and the deposition efficiency is lowered. Therefore, it is necessary for the treatment bath to have a nitrate component at a certain concentration or higher. This is also what was shown in (ii) above.
Precipitation of phosphate is caused by dissociation of the phosphoric acid component (H ₃ PO ₄ or H ₂ PO ₄ ⁻ ) in the solution into PO ₄ ³⁻ , so that phosphate (Zn ₃ (PO ₄ ) ₂ etc.) crystals Is formed as a film. Thus, if the state of phosphoric acid in the treatment bath is _{H 3 PO 4, H 2 PO} 4 - depending on whether it is, the process of precipitation (level, etc. of required energy) is different from clear. That is, it is easier to dissociate from H ₂ PO ₄ ⁻ to PO ₄ ³⁻ than to dissociate from H ₃ PO ₄ to PO ₄ ³⁻ . Thus, as a method of improving the electrolysis reaction efficiency, as much as possible the state of phosphoric acid contained in the processing bath, H ₂ PO ₄ ^- it is effective to a state containing a large amount of. That is, the treatment of the state in which the dissociation of H ₃ PO ₄ → H ₂ PO ₄ ⁻ is advanced by dissolving ZnO (zinc oxide) or the like in the solution state H ₃ PO ₄ and dissolving zinc ions (Zn2 +). By using a bath, the precipitation efficiency of phosphate can be improved.

  Other methods for increasing the electrolytic reaction efficiency will be described.

  The fact that the metal ion dissolved from the nitrate is 20 g / L or more is intended to increase the electrolytic reaction efficiency by increasing the electrolytic component ion concentration in the treatment bath.

In addition, the fact that the oxidation-reduction potential (ORP: hydrogen standard electrode potential) of the phosphate chemical treatment bath is 770 mV or more is an electrochemical reaction of iron.
Fe ²⁺ → (⇔) Fe ³⁺ + e ： 0.77v (1)
It is a control matter related to.
That the ORP of the treatment bath is 770 mV or more indicates that the state of iron ions in the treatment bath is all Fe ³⁺ from the formula (1). And it has shown that the iron ion in a processing bath does not change. Controlling the state of chemical components in the treatment bath is necessary to increase the reaction efficiency.

The current of 2 A / dm ² or more when the electrolysis voltage is 6 V or less shows the feature of this patent in comparison with the electrolysis treatment of the prior art (Patent Documents 1 and 2). In the prior art, there is no record of obtaining a current of 2 A / dm ² or more at 6 V or less.

Similarly, a current of 20 A / dm ² or more at an electrolysis voltage of 15 V or less indicates a feature of this patent in comparison with the electrolysis treatment of the prior art (Patent Documents 1 and 2). In the prior art, there is no record of obtaining a current of 20 A / dm ² or more at 15 V or less.

  Another object of the present invention is to newly apply the phosphate chemical conversion treatment to the warm forging or thermal forging lubrication treatment. That is, the following contents are provided as means for solving the problem.

(1)-phosphate; dissolved; was dissolved in-phosphate solution, zinc is a metal which can be dissolved by dissociating phosphate, iron or manganese; the skin membrane components as well as metal nitrate salts This is a treatment bath made up of a solution, anions other than nitrate ions and metal ions other than metal ions as film components are 0.5 g / L or less, and metal ions dissolved from nitrate are 20 g / L or more. In addition, an electrolytic phosphate chemical treatment bath in which phosphoric acid and phosphate ions are ½ or less of metal ions dissolved from the nitrate, and a metal to be a nitrate of the treatment bath is used as an electrode. An electrolytic phosphate chemical treatment method characterized by forming a film containing a metal precipitated from nitrate and phosphate by electrolysis with a treated product using a DC power source;
( 2 ) The electrolytic phosphate chemical treatment method according to ( 1 ), wherein a redox potential (ORP: hydrogen standard electrode potential) of the phosphate chemical treatment bath is 770 mV or more;
(3) In the electrolytic voltage is 6V or less, the electrolytic current is 2A / dm ² or more (1) or 2 electrolytic phosphate chemical treatment method according;
( 4 ) The electrolytic phosphate chemical treatment method according to (1) or (2), wherein the electrolysis voltage is 15 V or less and the electrolysis current is 20 A / dm ² or more;
( 5 ) At the time of hot forging or thermal forging of metal, it is obtained by the electrolytic phosphate chemical treatment method described in (1), and is composed of a metal and a phosphate having a melting point equal to or higher than the temperature applied to the material to be forged. that, Li down salts + metal, a conversion coating is formed on the surface of the forging material, using the forging to form a coating having a lubricating function by supporting a lubricant thereon to be forged material surface Lubricating method for warm or hot forging, characterized in that
( 6 ) The lubricating treatment method for warm or hot forging according to (5) , wherein the lubricant is an organic compound containing an organic fatty acid salt and an inorganic polymer compound having a multilayer structure;
( 7 ) The lubricating treatment method for warm or hot forging according to ( 6 ), wherein the lubricant is stearate, graphite, molybdenum disulfide or mica;
( 8 ) It is obtained by the electrolytic phosphate chemical treatment method according to (1) , and is composed of a metal and a phosphate having a melting point equal to or higher than a temperature applied to a material to be forged at the time of metal forging or thermal forging forming a re-emission salts + metal coating, a lubricant was supported, formed to be forging to form a coating having a lubricating function in warm forging or Netsu鍛processing thereon, the object to be forged A hot or hot forging method characterized by performing warm forging or hot forging, and a metal having a melting point equal to or higher than the temperature applied to the material to be forged during warm forging or thermal forging of metal Forging material with a coating film that has a lubrication function in warm forging or thermal forging process, in which a “phosphate + metal” film composed of and phosphate is formed, and a lubricant is supported on the film. Forming and heating the forging material, warm forging or Warm or hot forging method and performing between forging; and (9) Li down salts + metals, coatings, including phosphates containing no crystal water by differential thermal analysis (8 ) Warm or hot forging method as described
It is.

  The effect of the present invention is to provide an efficient method when a “metal + phosphate” chemical conversion film is formed by an electrolytic treatment method. That is, the present invention provides a method that allows a larger amount of current to flow than the conventional processing method, and thus shortens the processing time.

  The second effect of the present invention is that, when a chemical conversion film of “metal + phosphate” is formed by an electrolytic treatment method, the film can be formed by applying a voltage lower than that in the prior art. A "metal + phosphate" phosphate conversion coating can be formed by applying a voltage of 1.5 to 6 V, which has not been proven in the past. The ability to reduce the applied voltage suppresses decomposition of the treatment bath. Therefore, the stability of the treatment bath is greatly improved. Therefore, sludge generation is efficiently suppressed. Moreover, the crystal grain size of the film to be formed can be reduced by lowering the applied voltage. It is considered that reducing the crystal grains contributes to the improvement of corrosion resistance when used as a coating base.

  The third effect of the present invention is to apply to a new field by utilizing the properties of the chemical conversion film of “metal + phosphate”. It is possible to apply to warm forging lubrication. The phosphate chemical conversion film formed from the present invention has heat resistance. Therefore, a phosphate chemical conversion film was applied to the field of warm forging lubrication treatment that could not be applied with a film obtained from a conventional electroless treatment.

  This new lubrication treatment uses a phosphate chemical coating chemically reacted with the surface of the material to be forged, similarly to the cold forging lubrication treatment, and a lubricant is covered thereon. Therefore, materials that have not been conventionally applicable, such as organic fatty acid salts (for example, sodium stearate), can be used as a lubricant for warm forging.

  In addition, after heating the forged material to about 250 ° C., it is possible to apply it to a lubricant such as graphite that has been physically applied to the forged material without heating. And since the apply | coated lubricants, such as a graphite, adhere not to the heated iron surface but to a phosphate chemical conversion film, the adhesiveness to a forging material improves. This is a good tendency for lubricity.

The film formed by the electrolytic treatment of the present invention is “metal + phosphate”.
The metal is then dissolved and replenished in the treatment bath in the form of nitrate. And it reduces by electrolysis and precipitates. That is, it precipitates by the following formula (2).
M 2 ⁺ + 2e → M ⁰ (2)
Moreover, phosphoric acid dissociates and phosphate precipitates as a metal salt. The metal salt deposited at that time is limited to metal species that can dissociate and dissolve phosphoric acid. The metal species is limited to zinc, iron or manganese. However, in the present invention, the metal that can be used after the metal dissociates and dissolves phosphoric acid is preferably zinc from the viewpoint of ensuring the stability of the treatment bath.

First, the composition of the phosphating bath will be described.
The components constituting the phosphating bath include “phosphoric acid”, “part where zinc dissolves in a state of dissociating phosphoric acid and associates with phosphoric acid ions”, “nickel, cobalt, manganese, It is composed of a “dissolved portion of copper and zinc nitrate”. This can be classified into “phosphate ion system part” and “nitrate ion system part” if classified according to the type of anion. Other ionic species are miscellaneous ions, and are defined to 0.5 g / L or less.

  The phosphate chemical conversion bath of the present invention is expressed as a ratio of the above-mentioned types of anions in terms of the components constituting the treatment bath, and is expressed as nitrate ion system> phosphate ion system, and the metal of nitrate is 10 g / L or more. And the sum total of phosphoric acid and phosphate ion is 1/2 or less of nitrate metal.

More preferably, the phosphate chemical conversion bath of the present invention has a nitrate metal content of 20 g / L or more, and the total of phosphoric acid and phosphate ions is 1/2 or less of the nitrate metal.
In the electrolytic treatment of the aluminum material, it is allowed to contain F (fluorine) ions in an amount necessary for preventing the formation of an oxide film on the aluminum surface, for example, 1 g / L or less.

  Next, the electrode material will be described. The electrode material is a metal to be deposited. The metal that is reduced and deposited is the same metal that is replenished to the treatment bath as nitrate. Accordingly, the metal electrode materials used are nickel, cobalt, manganese, copper, and zinc or alloys of these metals.

Next, an electrolytic treatment method will be described. The electrolytic treatment is performed by forming an electrolytic treatment system as shown in FIG. 1 using the treatment bath, electrode material, and DC power source. Then, the electrolytic treatment is usually performed in the order of cathodic electrolysis using an object to be treated as an anode and an iron electrode as a cathode, and then using a metal that is a nitrate in the treatment bath as an anode and the object to be treated as a cathode. . In some cases, the anodization can be omitted. Also, the electrode material is generally different between anodizing and cathodic treatment, and a plurality of electrode materials can be used. Moreover, it is desirable that the electrolytic phosphate chemical treatment bath is usually provided with an electrolytic treatment bath and a tank that does not perform treatment, and is circulated between them. At that time, the structure should be such that molecular nitrogen oxides (NO _x ) generated with reduction of nitrate ions generated in the treatment bath can be removed.

Next, other ideas will be described. Treatment bath ORP: It is desirable to measure the oxidation-reduction potential and maintain it at 770 mV or higher. This is necessary to control the iron ions that dissolve from the electrode and workpiece during the treatment bath. The bath of ORP 770 mV or more from formula (1) does not contain Fe ²⁺ in principle. That is, when the treatment bath mainly containing nitrate ion of the present invention contains Fe ²⁺ (that is, when ORP is 770 mV or less), it is oxidized to Fe ³⁺ in the treatment bath, Solubility decreases and sludge is generated.

Therefore, maintaining the ORP of the treatment bath at 770 mV or more is to control the Fe ²⁺ in the treatment bath, that is, the amount of iron ions dissolved from the electrode and the object to be treated represented by the formula (3). is there.
Fe → Fe ²⁺ 2e (3)
Therefore, it is desirable to perform ORP control of the treatment bath.

  The electrolytic treatment is generally performed at 15 V or less. More preferably, it is 6 V or less.

  Next, as an application of the electrolytic phosphate chemical treatment of the present invention, there is an application to warm (or hot) forging lubrication treatment. The best mode will be described.

  The lubrication treatment for warm forging according to the present invention is such that a “phosphate + metal” coating composed of a metal and a phosphate having a melting point equal to or higher than the temperature applied to the material to be forged during the metal forging is forged. A forged material is formed on the surface of the material, on which a lubricant is supported, and a film having a lubricating function in warm forging is formed. And the phosphate film formation comprised from "phosphate + metal" formed on the surface of a to-be-forged material is performed by an electrolytic treatment system.

  The lubrication function in the metal forging process is that when the mold and the forged material (metal) come into contact with each other and the forged material changes in plasticity, the lubricating film (undercoat + lubricating film) covering the surface of the forged material is forged. It is to prevent the forging material and the mold from coming into direct contact by melting and fluidizing in the temperature range of processing and changing following the plastic deformation of the forging material. At that time, the base film that constitutes the lubricating film is generally an inorganic compound containing phosphate, and the lubricant is preferably an organic compound that usually softens between 200-1000 ° C. or an inorganic compound having a layered structure. It is. For example, organic fatty acid salts such as sodium stearate, fluororesin, molybdenum disulfide, graphite (graphite) and the like are preferably used.

  Phosphate compounds are selected as the base film for lubrication treatment in cold forging. The temperature of the cold forging process is selected, and the die and the forging material (metal) come into contact with each other and the forging material changes plastically. This is because the lubricating film (undercoat + lubricant film) covering the surface of the forged material melts and fluidizes in the temperature range of the forging process, and can change following the plastic deformation of the forged material. Therefore, the functions required of the phosphate chemical conversion film by cold forging are to maintain an appropriate adhesion to the material to be forged (metal) and a lubricant such as sodium stearate to be uniformly distributed.

  The lubricant is stable in the temperature range of the forging process when the mold and the forged material (metal) come into contact with each other and the forged material undergoes a plastic change without causing the lubricant to react with the counterpart mold. It is suitable to exist and have fluidity to follow plastic deformation (elongation) of the material to be forged, prevent direct contact between the mold and the material to be forged, and prevent the mold from deteriorating. is there.

Next, explanation will be made only on the ground treatment film for forging and lubrication. What is required for the undercoat is “maintaining adhesion to the metal” and “maintaining the lubricant uniformly”. If the lubricant can maintain adhesion to the base metal through a chemical reaction, the base treatment film is unnecessary. However, since such a lubricant does not exist, a ground treatment is required.
The adhesion to the material metal required for the base treatment is the temperature range of forging. When the mold and the forged material (metal) come into contact with each other and the forged material changes plastically, the surface of the forged material is changed. The covered lubricant film (undercoat film + lubricant film) is softened and fluidized in the temperature range of forging, and has an adhesiveness that changes following plastic deformation of the forged material.
Accordingly, the base treatment film is not suitable even if the adhesion to the base metal is too strong. Appropriate adhesion is required.

  Further, the surface treatment film is required to have a function of holding the lubricant uniformly. Common lubricants are organic fatty acid salts, multi-layer inorganic polymer compounds (graphite, etc.), etc. that do not have chemical affinity with the metal surface (thus, the lubricant is formed directly on the metal. I can't do it.) On the other hand, since phosphate has chemical affinity with the above-described lubricant, the lubricant can be retained.

  As described above, the lubricating ground treatment film is interposed between the base metal and the lubricant having different chemical properties and plays a role of bonding the two. This is an important feature.

What should be considered in the forging lubrication process is the temperature region. The forging process is performed at different temperatures depending on forging methods such as cold forging, warm forging, and hot forging. Moreover, the warm forging differs in the processing temperature with the kind of metal. Therefore, the classification of lubricity and fluidity in the temperature range of forging is generally as follows.
Forging-(i) Cold forging: Processing temperature 100-250 ° C
(Ii) Warm forging process (ii-1) Steel: Processing temperature 300-1000 ° C
(Ii-2) Nonferrous metal: Processing temperature 200-600 ° C
Therefore, the lubricating treatment (undercoat film + lubricant film) is also applied with reference to the above temperature.

  Currently, phosphate compounds are selected as the base film for cold forging and lubrication of steel. When the forged material changes plasticity due to contact between the mold and the forged material (metal) in that temperature range, the forged material This is because the lubricating film (base film + lubricating film) covering the material surface is softened and fluidized in the temperature range of the forging process, and can function to change following the plastic deformation of the material to be forged. Therefore, the functions required for the phosphate chemical coating in the cold forging lubrication treatment are appropriate adhesion to the material to be forged (metal) and uniform distribution and retention of the lubricant.

  Now, when considering a lubricating base film applicable to warm forging, it is necessary to consider the forging temperature. That is, it is desired to follow the plastic deformation of the material without the base film being detached from the material even when heated to 200 ° C. or higher. The chemical affinity of the phosphate chemical film with the lubricant has been confirmed conventionally. However, the film obtained from the conventional electroless treatment has not been applied to the warm-forging ground treatment. This is because when the workpiece is heated to 200 ° C. or higher, the phosphate chemical conversion film is decomposed and detached from the workpiece.

The phosphate chemical conversion coating obtained from the conventional electroless treatment is in the form of large crystal grains of about 50 μm containing water of crystallization such as Zn ₃ (PO ₄ ) ₂ .4H ₂ O. Along with this, it is presumed that crystal water is detached and the chemical structure of the film of large crystal grains is destroyed. Therefore, the phosphate chemical conversion film formed by electroless treatment does not have heat resistance.

  It is desirable that the phosphate chemical coating applied to the warm forging lubrication treatment has heat resistance. And the "phosphate + metal" chemical conversion film obtained by the electrolytic treatment of this invention has heat resistance applicable to a warm forging process. The coating is a coating that contains a large amount of metal that has been reduced and deposited, and that contains phosphate.

  Further, the film formed from the electrolytic treatment of the present invention is a “phosphate + metal” chemical conversion film, and since it contains a phosphate, it has an affinity for a lubricant. As described above, the film of the present invention has the characteristics of having both heat resistance and affinity for the lubricant.

  Such a film can be formed after following the use of a treatment bath containing no metal ions other than the film components shown in Patent Document 1.

  That is, the lubrication treatment for warm forging according to the present invention is the formation of a phosphate film composed of “phosphate + metal” formed by electrolytic treatment on the surface of the material to be forged. Phosphoric acid and phosphate ions A zinc ion which is a metal capable of dissociating and dissolving phosphoric acid; and a solution in which nickel, cobalt, manganese, copper or zinc nitrate is dissolved; This is done by electrolysis.

  Preferably, in the phosphate film formation composed of “phosphate + metal” formed on the surface of the material to be forged, metal ions dissolved from nitrate are 10 g / L or more, and phosphoric acid and Phosphate ions are performed in a treatment bath that is 1/2 or less of the metal ions. More preferably, in the formation of a phosphate film composed of “phosphate + metal” formed on the surface of the material to be forged, metal ions dissolved from nitrate are 20 g / L or more, and phosphoric acid and phosphorus The acid ion is performed in a treatment bath that is 1/2 or less of the metal ion dissolved from the nitrate.

  Next, application of the above-mentioned film to warm forging will be described. In the present invention, examples of steel materials are mainly described as described above, but the present invention can be applied to all metal materials for performing warm forging.

  Hot forging is a process in which a metal material is forged after being heated to a temperature higher than room temperature. The heating temperature varies depending on the type of metal. Table 2 shows general warm forging and thermal forging temperatures of various metals subjected to warm forging.

  Next, the metal characteristics of the “phosphate + metal” film formed on the material to be forged and the conditions of the treatment bath are clarified. Table 3 lists metals that can be included in the phosphate conversion coating.

  The first necessary condition for a metal corresponding to “phosphate + metal” is the melting point of the metal. The metal contained in the film needs to have a melting point equal to or higher than the warm forging temperature of the material to be forged. (See Table 2)

The second necessary condition relates to the behavior in the treatment bath for forming a film. In order for the metal to be taken into the coating, it is necessary that the metal is stably dissolved and present as a divalent metal ion in the phosphate chemical treatment bath. For this purpose, it is necessary that the charge of the metal does not easily fluctuate within the range of the oxidation-reduction potential where the solvent water does not decompose. That is, there is no equilibrium of M ²⁺ ⇔ M ³⁺ + e.
(Metal ions, M ²⁺ → M ³⁺ + solubility becomes M ³⁺ in e is reduced. Therefore, sludge is produced in a treatment bath. This inhibits the stability of the solution of the treatment bath (This is what is to be done and is not acceptable.)

The third necessary condition is that the solvent is not affected by electrolysis of water. Decomposition of water by an electrochemical reaction occurs when the potential of the treatment bath exceeds the oxidation-reduction potential represented by the following formulas (4) and (5).
Anode ^{_{reaction: H 2 + 2OH - ⇔ 2H}} 2 O + 2e: -0.83V (4)
Cathode reaction: 0 ₂ + 4H ⁺ + 4e ⇔ 2H ₂ O: 1.23V (5)
Therefore, if the M ²⁺ ⇔ M ³⁺ + e equilibrium potential of the metal component in the treatment bath is within the range of the potentials shown in equations (4) and (5), the metal component ion is Among them, there is a possibility of changing from the M ²⁺ state to the M ³⁺ state. It is undesirable for such fluctuations to occur.
Metals listed in Table 3 does not have a M ²⁺ ⇔ M ³⁺ + e equilibrium potential in the range of -0.83V～1.23V.

The fourth requirement is that cathode deposition can be performed without being affected by electrolysis of water as a solvent. This should take into account M ⇔ M ²⁺ + 2e in Table 3. That is, cathode deposition of metal ions: When M ²⁺ + 2e → M is −0.83 V or less, the reaction of the cathode decomposition reaction formula (4) of water as a solvent occurs preferentially, so that cathode deposition of metal ions occurs. Is impossible in principle. That is, if the metal deposition-dissolution reaction potential in Table 3 is significantly lower than −0.83 V, electrolytic deposition from an aqueous solution is impossible. The metals (Ni, Mn, Co, Cu, Zn) listed in Table 3 can be deposited because the deposition-dissolution reaction potential is −0.83 V or more except for Mn. The potential of Mn is slightly below −0.83 V and can be deposited.

  Therefore, since the metals listed in Table 3 satisfy the above three conditions, a “phosphate + metal” chemical conversion film can be formed by electrolytic treatment. However, it is necessary to use the deposited metal in a timely manner according to the type of material to be forged.

  Next, the function and optimum form of the lubricant will be described. As the lubricant to be formed on the object to be treated, those conventionally used for warm forging: for example, graphite can be used in the present invention. Organic fatty acid salts can also be used as novel lubricants for warm-forged workpieces. This is because a phosphate chemical conversion film having heat resistance is used as a base treatment for the lubricant.

  The function of the lubricant is to prevent direct contact between the workpiece and the mold during warm forging. In the case of steel, graphite (graphite) is used as a lubricant that is heated to about 250 ° C. and then applied directly to the forging. However, the graphite applied there is only physically attached to the material to be forged and does not have reliable adhesion. Therefore, the material to be forged is immediately heated to about 800 ° C. and subjected to warm forging.

  If a phosphate chemical conversion film having heat resistance is formed as the base film, the formation of the lubricating film on the material to be forged becomes easy. This is because the lubricant has chemical affinity (similar in nature) to the phosphate conversion coating. Therefore, compared with the steel material surface, the surface of the chemical conversion film can make the lubricant uniformly dispersed and adhere securely.

  In the warm forging method of the present invention, a phosphate chemical conversion film having heat resistance is formed, and a lubricant is applied thereon. Therefore, it is possible to use an organic fatty acid salt as a new lubricant. That is, a fatty acid salt such as sodium stearate conventionally used in cold forging can be used.

  In other words, the hot forging lubrication treatment of the present invention forms a “phosphate + metal” film composed of a metal and a phosphate having a melting point equal to or higher than the temperature applied to the material to be forged during the hot forging of metal. And forming a forging material on which a film having a lubricating function in a warm forging process is formed by supporting a lubricant which is an organic fatty acid salt, an inorganic polymer compound having a multilayer structure, and the like. And warm forging. And warm forging itself can be performed in principle by the same method as the present condition. Lubricant spraying on the mold during warm or hot forging is also necessary because it has a function of cooling the mold.

Examples 1-5
(I. Efficiency improvement of electrolytic phosphate chemical treatment)
Table 4 shows the treatment bath conditions of Example 1-5 and Comparative Example 1.

  In the comparative example, the phosphoric acid and phosphate ion concentration is 1/2 or more of the metal ion (Ni). Therefore, it is not the treatment bath of the present invention in that respect.

Electrolytic phosphate chemical conversion treatment was performed in these treatment baths. Table 5 shows the outline.
The film thickness is measured with an electromagnetic film thickness meter (Kett Science Laboratory: LE-300J).
2 to 7 show SEM photographs (1000 times) of the films formed in Examples 1 to 5 and Comparative Example 1, respectively. In Example 1, since the voltage is small, the current is small and the film formation is not sufficient. In Examples 2 to 5, a film is formed.

Comparative Example 1 is an implementation result in a mass production facility. Table 6 shows the steps of the comparative example.
Comparative Example 1 uses a clutch component stator as an object to be processed. FIG. 8 shows an appearance after 2000 hours of salt spray test after chemical conversion treatment → electrodeposition coating (film thickness: 15 μm). There is no peeling of the coating film from the coating film cross-cut portion, and the corrosion resistance is good.
The paint is Nippon Paint "Power Nix" 110 Black: Lead-free cationic electrodeposition paint.

Next, the electrodeposition coating of Examples 1 to 5 will be described.
Electrodeposition: Power Nix 110 Black (lead-free cationic electrodeposition)
Painting conditions: The following three types are applied.
B: Electrodeposition coating time: 45 seconds (including rising voltage control 10 seconds)
B: Electrodeposition coating time: 60 seconds (including rising voltage control 11 seconds)
C: Electrodeposition coating time 90 seconds (including rising voltage control 12 seconds)
Coating temperature: 30 ° C Baking and drying temperature: 160 ° C x 10 minutes
Painting voltage: 150V

Table 7 shows the coating film thickness of each example after coating → baking. (Display is μm)
The coating film thickness greatly depends on the electrodeposition coating time rather than the conditions for forming the chemical conversion film.

Table 8 shows the results of the salt spray test on the coated products. The numbers shown in Table 8 are values in which the peel width from the line obtained by cutting the coating film is expressed in mm. A smaller display value is better.
The results in Table 8 indicate that the coating corrosion resistance is more dependent on the chemical conversion treatment conditions than the coating film thickness. In the examples of the electrolytically treated products, the coating corrosion resistance is at the current level even if the coating film thickness is small except for the voltage of 1.8V.

It can be seen that the examples of this patent can be processed in 1/2 processing time (chemical conversion treatment, electrodeposition coating, baking time) of the comparative example. This is possible by the combination of the above coating conditions (a) and Example 1-5. In the combination, the coating film thickness is also 1/2 of that of the comparative example, but the corrosion resistance can maintain the level of the comparative example 1.
And the electrolysis voltage is 3-6v, and a process with a voltage lower than 8v of Comparative Example 1 is possible. Therefore, in terms of electrolytic voltage, the decomposition of the treatment bath components is suppressed. That is, it becomes the direction which can suppress sludge production | generation more.

Examples 6-8
(II. Application to warm forging)
Car engine parts (lower body: material SCM415) were used. FIG. 9 shows a state before warm forging, and FIG. 10 shows a state before and after warm forging.
Table 9 shows the steps of hot forging of Examples 6 to 8 and Comparative Example 2. However, water washing and hot water washing are omitted. Further, in Examples 6-8 and Comparative Example 2, in the hot forging press, a solid lubricant (graphite) was spray-applied to the press mold under the same conditions.
The difference between Examples 6 to 8 is only the difference in the type of lubricant. Moreover, the difference between Examples 6-8 and Comparative Example 2 is that the example includes shot blasting (implemented by removing the phosphate chemical conversion treatment film in the previous step), and the forged material contains “metal + phosphate” While the ground treatment and the lubrication treatment are performed, the conventional example does not carry out these treatments.
The details of the electrolytic phosphate chemical treatment are as follows. The composition of the treatment bath is phosphoric acid and phosphate ions: 15 g / L, zinc ions: 10 g / L, Ni ions: 51 g / L, and nitrate ions: 157 g / L. In this treatment bath, an object to be treated (lower body) shown in FIG. 9 is used as a cathode, and a Ni plate is used as an anode. After immersion without applying voltage for 10 seconds, the voltage is increased to 13 V in 5 seconds, and a current is passed for 28 to 32 A × 25 seconds per 1 object (surface area of 1.2 dm ² ). The temperature at that time is 30 to 34 ° C. In this way, a black gray phosphate + Ni film is formed on the surface of the workpiece.
In addition, the lubrication treatment is immersed in an aqueous solution to form a film. The summary is shown in Table 10.
Table 11 shows the difference in processing load in the warm forging press.
The working load was greatly different between the example and the comparative example. In the example, the processing load is low and good. This indicates that the lubrication performance is significantly different between the forged material formed with the lubricating film (Example) and the case where the lubricating film is not formed (Comparative Example). It is clear that the present invention is effective.
(III. Comparison of composition of phosphate conversion coating)
It shows that Examples 6 to 8 of the present invention are different from the conventional electrolytic phosphate chemical conversion coating. Examples 1 and 4 of JP-A No. 2000-234200 are listed as Comparative Example 3 as a film obtained by conventional electrolytic treatment (Comparative Example 3).
The difference between Examples 6 to 8 and Comparative Example 3 is the ratio of the metal component to phosphoric acid or phosphorus (P) in both the treatment bath composition and the film composition. In both the treatment bath composition and the film composition, the examples of the present invention have a higher metal component ratio than Comparative Example 3. That is, the film of the present invention is a film having a large metal component. In any case, the difference from the conventional example is clear.
(IV. Comparison of heat resistance of phosphate chemical coating)
Next, the heat resistance of the film is shown by DSC: differential thermal analysis result.
Fig. 11: Differential thermal analysis diagram of Examples 6 to 8 (phosphate coating for warm forging from electrolytic treatment) Fig. 12: Differential thermal analysis diagram of Comparative example 4 (phosphate coating from electroless treatment) Comparative example 4 is a film prepared by a conventional electroless method. The phosphate chemical conversion bath is prepared by adjusting Nippon Parkerizing Co., Ltd. chemical conversion chemical: “PALBOND” 3684X to predetermined conditions. A cold-rolled steel sheet was immersed in the treatment bath (80 ° C.) for 10 minutes to form a film. FIG. 12 is a differential thermal analysis diagram of the coating, and FIG. 14 is an SEM diagram of the coating.
FIG. 11 is a differential thermal analysis diagram of the phosphate chemical conversion film composition used in Examples 6 to 8 of the present invention. That is, it is a phosphate chemical conversion film prepared by electrolytic treatment for warm forging of steel materials.
FIG. 12 is a differential thermal analysis diagram of a conventional phosphate conversion coating film composition that is currently used for cold forging of steel. That is, it is a differential thermal analysis diagram of a phosphate film obtained by an electroless treatment method.
The major difference between FIG. 11 and FIG. 12 is that there is a change in the differential scanning calorific value curve in the temperature region below 200 ° C. in FIG. 12, whereas such a phenomenon is not seen in FIG.
The film from the electroless treatment in FIG. 12 undergoes a large weight change (decrease) with a temperature increase up to 200 ° C. This change in the large differential scanning calorimetry curve indicates a large change in the film structure. It is known that the phosphate chemical conversion film obtained by conventional electroless treatment exists in the form of crystals containing water crystals (hydrous salts): Zn ₃ (PO ₄ ) ₂ · 4H ₂ O. . Therefore, the large change in the film structure is due to the fact that water crystals are removed from the phosphate crystals by heating up to 200 ° C. Moreover, when FIG. 13 and FIG. 14 are seen, it is clear that the film appearance differs between the electrolytic treatment and the electroless treatment. This difference in appearance is considered to be related to the structure of the film.
For this reason, it is impossible to apply a phosphate chemical conversion film formed by conventional electroless treatment to a base film for warm forging that is heated to 500 ° C. or higher. Therefore, the conventional phosphate chemical film has not been used for warm forging.
The result of differential thermal analysis shows the change in the weight of the film due to heating. The film formed by electroless treatment (FIG. 12) has a weight loss of 9.78 / 11.062 = 0.84 up to the absorption of the differential scanning calorimetry curve at 170 ° C., but the electrolytic treatment film (FIG. 11) of the present invention has 187 Even a slight change in ℃ keeps the decrease to 13.57 / 13.804 = 0.983. This indicates that the phosphate chemical coating of the present invention is heat resistant and more effective than conventional coatings.
Example 9
(Example using organic fatty acid salt as lubricant)
Automobile engine parts (NB cylinder: material SUJ2: alloy steel containing chromium) were used.
FIGS. 15 and 16 show the form of the NB cylinder before and after warm forging, respectively.
Table 13 shows the hot forging process of Example 9 and Comparative Example 5.
In the hot forging press, in both Example 9 and Comparative Example 5, the lubricant was spray applied to the press mold under the same conditions.
Also, the difference between Example 9 and Comparative Example 5 is that after Example 9 performs shot blasting (implemented by removing the phosphate chemical conversion treatment film in the previous step), the “metal + phosphate” is added to the forged material. Whereas the surface treatment and the lubrication treatment were carried out in the sodium stearate solution, Comparative Example 5 was not carried out.
The electrolytic phosphate chemical treatment of Example 9 is the same as that of Examples 6-8.
Table 14 shows the processing load in the hot forging press.
The working loads of Example 9 and Comparative Example 5 are equivalent. Example 9 is an example in which sodium stearate was used as a lubricant for the forged material. This is a thing with no track record as a lubricating film in the conventional forging material. The present invention shows an example in which inexpensive sodium stearate can be applied to a lubricating treatment.

The electrolytic phosphate chemical treatment method of the present invention can apply a large current at a lower voltage than the conventional electrolytic treatment. That is, this is an electrolytic phosphate chemical conversion technique that is more efficient than conventional techniques.
In addition, the present invention is effective with respect to the lubricating process for warm forging. Conventionally, phosphate conversion coatings could not be used as a base treatment for lubricants, but using the method of depositing a large amount of the metal of the present invention, a coating applicable to warm forging was developed, and a new warm A forging lubrication system was developed. It was confirmed that the developed lubrication treatment significantly reduced the processing load during warm forging. Therefore, it is a technology that enables innovation of warm forging.

The figure which shows the electric current and ion flow in an electrolysis process. The SEM photograph (1000 times) of the membrane | film | coat formed in Example 1. FIG. The SEM photograph (1000 times) of the film | membrane formed in Example 2. FIG. The SEM photograph (1000 times) of the film | membrane formed in Example 3. FIG. The SEM photograph (1000 times) of the film | membrane formed in Example 4. FIG. The SEM photograph (1000 times) of the film | membrane formed in Example 5. FIG. The SEM photograph (1000 times) of the film | membrane formed in the comparative example 1. FIG. Appearance after 2000 hours of salt spray test after chemical conversion treatment, electrodeposition coating (film thickness 15μ). Schematic of a material to be forged (lower body). The state before and after the warm forging process of a to-be-forged material (lower body) is shown. The differential thermal analysis figure of the phosphate chemical conversion film used for Examples 6-8 of this invention. The differential thermal analysis figure of the phosphate chemical conversion film of the comparative example 4. The SEM figure of the phosphate chemical conversion film of Examples 6-8. The SEM figure of the phosphate chemical conversion film of the comparative example 4. The state (NB cylinder) before and after the warm forging process in Example 9 is shown. The state (NB cylinder) before and after warm forging in Comparative Example 5 is shown.

Claims (9)

-Phosphate; dissolved in-phosphate solution, zinc is a metal which can be dissolved by dissociating phosphate, iron or manganese; from a solution obtained by dissolving, to become a metal nitrate salt skin layer components as well A treatment bath composed of anions other than nitrate ions and metal ions other than metal ions as film components of 0.5 g / L or less, metal ions dissolved from nitrates of 20 g / L or more, and Phosphoric acid and phosphate ions use an electrolytic phosphate chemical treatment bath that is 1/2 or less of the metal ions dissolved from the nitrate, and the metal that becomes the nitrate of the treatment bath is used as an electrode. An electrolytic phosphate chemical treatment method characterized in that a film containing a metal precipitated from nitrate and a phosphate is formed by electrolysis using a direct current power source. The redox potential of the phosphate chemical treatment bath (ORP: hydrogen standard electrode potential), the electrolytic phosphate chemical treatment method according to claim 1 Symbol placement is at least 770 mV. 3. The electrolytic phosphate chemical treatment method according to claim 1 or 2, wherein the electrolysis voltage is 6 V or less and the electrolysis current is 2 A / dm ² or more. The electrolytic phosphate chemical treatment method according to claim 1 or 2, wherein the electrolysis voltage is 15 V or less and the electrolysis current is 20 A / dm ² or more. In the warm forging or Netsu鍛working metal, obtained in the electrolytic phosphate chemical treatment method according to claim 1, wherein, made of metal phosphate salt having a temperature above the melting point applied to the forging material, Li It is characterized by using a forging material in which a chemical conversion film of phosphate + metal is formed on the surface of the material to be forged, and a film having a lubricating function is formed on the surface of the material to be forged by supporting a lubricant thereon. Lubricating method for warm or hot forging. 6. The lubricating treatment method for warm or hot forging according to claim 5 , wherein the lubricant is an organic compound containing an organic fatty acid salt and an inorganic polymer compound having a multilayer structure. The lubricating treatment method for warm or hot forging according to claim 6 , wherein the lubricant is stearate, graphite, molybdenum disulfide or mica. Obtained in electrolytic phosphate chemical treatment method according to claim 1, wherein, made of metal phosphate salt having a temperature above the melting point applied to the forging during hot forging or Netsu鍛working metal,-phosphate A forging material is formed which forms a film of salt + metal , and has a lubricating function in warm forging or thermal forging, on which a lubricant is supported, and this forging material is heated. A warm or hot forging method characterized by performing warm forging or hot forging. Li down salts + metals, coating of claim 8 warm or hot forging method further comprising a phosphate containing no crystal water by differential thermal analysis.