JP3985724B2 - Method for producing rare earth-transition metal-nitrogen alloy powder - Google Patents

Description

[0001]
[Industrial application fields]
The present invention relates to a novel method for producing not only intermetallic compound powders but also alloy powders containing rare earth elements, and particularly relates to alloy powders having high magnetic properties.
[0002]
[Prior art]
In general, an intermetallic compound or alloy of a rare earth element and a transition metal such as Fe, Co, or Ni is an industrially useful material. For example, a thin film of Tb—Fe—Co is used as a magneto-optical memory, and Sm—Co is used as a permanent material. For magnets, La-Ni is used for hydrogen storage alloys. In this case, these intermetallic compounds or alloys are often required in a powder state. In order to obtain a powder, a method is generally used in which a component metal is melted into an ingot and then the ingot is pulverized.
[0003]
The magnetic substance has a unique single domain particle size, and the coercive force is maximized by making the particle size of the magnetic powder close to the single domain particle size. In the rare earth element-transition metal magnetic material, the single domain particle diameter is several μm. Therefore, a technology for producing fine particles is indispensable for the alloy powder as a magnetic material in order to improve magnetic characteristics.
[0004]
On the other hand, a reduction diffusion method is known in which rare earth oxide powder and transition metal powder are mixed and heated in calcium vapor to reduce the rare earth oxide and diffuse it into the transition metal. (JP-A 61-295308, JP-A 5-148517, JP-A 5-279714, JP-A 6-81010) The reduction diffusion method uses an inexpensive rare earth oxide, There is an advantage that the alloy can be formed simultaneously with reduction, and this method is widely used in the production of SmCo5 intermetallic compound or Sm-Co alloy for permanent magnets.
[0005]
This method has not yet been a sufficient method for obtaining a fine magnetic powder corresponding to a single magnetic domain particle size. This is because the particle size of the iron group metal as a raw material is considerably larger than that of the rare earth element oxide. In order to obtain a magnetic powder having a single magnetic domain particle size, it is necessary to optimize the particle size of the iron group transition metal used as a raw material, and the optimum particle size will be about 1 μm.
[0006]
[Problems to be solved by the invention]
Accordingly, an object of the present invention is to provide a rare earth ferromagnetic powder (alloy powder) that can optimize the particle size of a transition metal used as a raw material and obtain a magnetic powder having a high magnetic performance close to a single domain particle size. It is to be.
[0007]
Furthermore, another purpose is to increase the reactivity by thoroughly mixing rare earth elements, which are the main constituent elements of the alloy powder, and transition metal elements such as Fe, Co, Ni, etc., so that the composition in the alloy powder is uniform. An object of the present invention is to provide a permanent magnet having a magnetic property having a high coercive force by suppressing generation of an unnecessary phase as a magnetic material.
[0008]
[Means for Solving the Problems]
As a result of diligent research to solve the above problems, the inventors of the present invention dissolved and ionized rare earth elements and transition metals such as Fe, Co, and Ni with acids, etc., and mixed them completely in a solution state. By precipitating the ions by a precipitation reaction, it was found that the obtained precipitate was a very good alloy powder raw material with a very good mixing state, and the present invention was completed.
[0009]
That is, the method for producing an alloy powder of the present invention has the following features (1) to (13).
[0010]
(1) In a method for producing an alloy powder comprising a rare earth element and at least one transition metal selected from Fe, Co and Ni, from at least one cation of the rare earth element and Fe, Co and Ni A step of reacting at least one cation selected from the group consisting of these cations and a substance that forms an insoluble salt in a solution to precipitate a precipitate;
Calcination of the precipitate to obtain a metal oxide;
Heating the metal oxide in a reducing atmosphere
It is characterized by including.
[0011]
(2) A precipitate composed of precipitate particles having a uniform distribution of constituent elements, a sharp particle size distribution, and a uniform particle shape is fired to obtain a metal oxide, and the metal oxide is heated in a reducing atmosphere. The manufacturing method of the alloy powder characterized by including a process.
[0012]
(3) The average particle size of the precipitate particles is 0.05 to 20 μm, and the total particle size has a particle size and particle size distribution in the range of 0.1 to 20 μm. The manufacturing method of the alloy powder of description.
[0013]
(4) The method for producing an alloy powder according to (1), wherein a precipitate that is present in a state where the rare earth element and the transition metal element are sufficiently mixed in the precipitate particles is used.
[0014]
(5) The method for producing an alloy powder according to (1), wherein the precipitate is easily burned or decomposed by heating in the atmosphere at a high temperature to produce a metal oxide.
[0015]
(6) In the step of firing the precipitate, the firing atmosphere is in the air or oxygen richer than the air, The method for producing an alloy powder according to (1).
[0016]
(7) The substance that forms an insoluble salt with at least one ion selected from the group consisting of at least one rare earth element element and Fe, Co, and Ni contains oxygen in the composition ( The manufacturing method of the alloy powder as described in 1).
[0017]
(8) The production of the alloy powder according to (7), wherein the substance that forms the insoluble salt is at least one of hydroxide ions, carbonate ions, bicarbonate ions, and oxalate ions. Method.
[0018]
(9) The alloy according to (2), comprising a step of reducing a metal oxide in which the rare earth element and the transition metal are sufficiently mixed in the particles and inheriting the particle shape and particle size distribution of the precipitate particles. Powder manufacturing method.
[0019]
(10) The reduction of the metal oxide includes a step of heating the metal oxide in a reducing gas atmosphere, and then a step of mixing and heating a reducing substance having a reduction potential more negative than that of the rare earth element. The method for producing an alloy powder according to (1), comprising a step process.
[0020]
(11) The reduction in the reducing gas atmosphere is characterized in that the heating temperature is in the range of 300 to 900 ° C., and 40% or more of the stoichiometric amount of oxygen with respect to the transition metal is reduced and removed (10) The manufacturing method of the alloy powder as described in 2.
[0021]
(12) The metal oxide and B are sufficiently mixed and reduced with a reducing gas, and then reduced and diffused with a reducing agent, or the metal oxide is reduced with a reducing gas, The method for producing an alloy powder according to (1), wherein a stoichiometric amount of B is mixed to perform reduction diffusion.
[0022]
(13) After the reduction reaction by the reducing agent is completed, nitrogen gas or a compound gas that can be decomposed by heating to supply nitrogen is introduced in the same furnace at a temperature in the range of 300 to 600 ° C. The method for producing an alloy powder according to (1), which is characterized in that
[0023]
DETAILED DESCRIPTION OF THE INVENTION
The subject of the present invention is an alloy powder comprising a rare earth element and a transition metal such as Fe, Co and Ni, and the present invention can also be applied to an intermetallic compound. The rare earth element refers to at least one of rare earth elements including light rare earth and heavy rare earth, that is, Y, Nd, Pr, La, Ce, Tb, Dy, Ho, Er, Eu, Sm, Gd, Er, Tm. , Yb, and Lu, and the rare earth oxide powder refers to these oxides, double oxides, and mixtures thereof. Therefore, the present invention can be applied to, for example, Pr—Ni, Sm—Co, Nd—Fe—Co, and Ce—Fe as alloy powder, and a part of the composition is B (boron) or N ( Nd-Fe-B, Sm-Fe-N, Nd-Fe-N, Nd-Fe-NB, Ce-Fe-N, Pr-Fe-N, etc. alloys or metals It can also be applied to intermetallic compounds. It can also be applied to the production of alloys of rare earth elements and transition elements other than these.
[0024]
In the production method of the present invention, the constituent cation is uniformly mixed in a solvent. Therefore, it is necessary to prepare a solution in which rare earth elements and transition metals, which are constituent components of these alloys, are dissolved. An acid aqueous solution can be used as a solvent that can ionize and dissolve these metal elements in common. Preferred acids include mineral acids such as hydrochloric acid, sulfuric acid, and nitric acid, and can dissolve the above metal ions at a high concentration. Further, as another method for preparing the metal element solution, it is also possible to dissolve chlorides, sulfates and nitrates of these constituent metals in water. The solution is not limited to an aqueous solution, but may be a solution in which an organic metal such as a metal alkoxide is dissolved in an organic solvent such as alcohol, acetone, cyclohexane, tetrahydrofuran, or the like.
[0025]
Anions (nonmetal ions) such as hydroxide ions, carbonate ions, and oxalate ions can be preferably used as substances that generate salts insoluble with these ions from a solution in which the metal ions are dissolved. That is, a solution of a substance that can supply these ions can be used. For example, oxalic acid can be used as a substance for supplying oxalate ions such as ammonium bicarbonate and sodium bicarbonate as a substance for supplying carbonate ions as a substance for supplying hydroxide ions such as ammonia and caustic soda. In the case of a solution in which a metal alkoxide is dissolved in an organic solvent, a precipitate can be deposited in the form of a metal hydroxide by adding water. In addition, any substance that reacts with a metal ion to produce an insoluble salt can be applied to the present invention. As a method for producing an insoluble salt of hydroxide, a sol-gel method can be preferably used.
[0026]
By controlling the reaction between metal ions and non-metal ions, it is possible to obtain an ideal alloy powder raw material with a uniform distribution of constituent elements in the precipitate particles, a sharp particle size distribution, and a well-defined particle shape. it can. The use of such raw materials improves the magnetic properties of the final product alloy powder (magnetic material). This precipitation reaction can be controlled by appropriately setting the supply rate of metal ions and non-metal ions, the reaction temperature, the reaction solution concentration, the stirring state of the reaction solution, the pH during the reaction, and the like. To set these conditions, first select the best yield of the precipitate, and observe the microscope for the independence (particle shape) of the precipitate particles and the sharp particle size distribution of the precipitate particles. While determining each condition. Needless to say, the form of the precipitate varies greatly depending on what kind of chemical species is selected as a raw material and what kind of precipitation reaction is applied. By this precipitation step, the particle diameter, particle shape, and particle size distribution of the alloy powder as the final magnetic material are approximately determined. As described above, the control of the precipitation reaction is very important in that the particle performance is closely reflected in the magnetic material. It is preferable that the particle size of the precipitate particles is 0.05 to 20 μm, and preferably the size and distribution so that almost all the particles are in the range of 0.1 to 10 μm. Moreover, it is preferable that an average particle diameter exists in the range of 0.1-10 micrometers. In the precipitate particles obtained in this way, the rare earth element and the transition metal element are present in a sufficiently mixed state.
[0027]
In the present invention, the precipitate obtained from the precipitation reaction is calcined to produce a metal oxide. Usually, the deposit is calcined after removing the solvent prior to calcining. This is because if the solvent is sufficiently removed in this step, firing is easy. In addition, when the precipitate has a high solubility in a solvent at a high temperature, it is particularly necessary to remove the solvent sufficiently. This is because the precipitate particles are dissolved, the particles are aggregated, and the particle size distribution and particle size are adversely affected.
[0028]
At the time of firing the precipitate, an insoluble salt composed of metal ions and non-metal ions is heated, so that the non-metal ions are decomposed to generate a metal oxide. Therefore, this firing is preferably performed under oxygen-rich conditions. In addition, it is preferable to select one containing oxygen as a constituent element of the nonmetallic ion. Such include hydroxide ions, bicarbonate ions, oxalate ions, citrate ions and the like. Conversely, sulfide ions and the like are ions that cause precipitation in common with these metals, but are not suitable because they do not easily decompose into oxides because they do not contain oxygen. Phosphate ions, borate ions, silicate ions, etc. are also substances that form insoluble salts with rare earth ions, transition metal ions, but phosphates, borates, and silicates are easily oxidized by subsequent firing. It does not generate a product and is difficult to apply to the present invention. Therefore, the non-metal ions that can be preferably applied to the precipitation reaction constituting the present invention include inorganic salts that can easily generate oxides when heated, such as hydroxide ions, carbonate ions, oxalate ions, and the like. It is an insoluble organic salt that burns easily. In addition, when an insoluble organic salt is hydrolyzed with water like an alkoxide to form a hydroxide, it is preferable to heat it once as a hydroxide.
[0029]
Since the main point of this baking is to decompose the non-metallic ions to obtain a metal oxide, the baking temperature is also set at a temperature equal to or higher than the temperature at which such decomposition reaction occurs. Therefore, although the firing temperature varies depending on the type of metal ion and the type of nonmetal ion, it is appropriate to fire at a temperature of 800 to 1300 ° C. for several hours, more preferably in the range of 900 to 1100 ° C. To do. In this case, it is preferable that the atmosphere of the furnace is sufficiently blown with air using a blower or the like, or oxygen is introduced into the furnace and fired.
[0030]
By this firing, a metal oxide in which the rare earth element and the transition metal element are microscopically mixed in the particles can be obtained. This oxide particle is an oxide having a very good particle performance that inherits the shape distribution of the precipitate particles as it is.
[0031]
In order to obtain an alloy powder from a metal oxide, a reduction reaction is basically applied. Here, even if it is simply called a metal oxide, the metal oxide is a transition metal of rare earth elements and Fe, Co, and Ni. The reduction potentials of Fe, Co, and Ni are −0.447v, −0.28v, and −0.257v, respectively, with respect to the standard hydrogen electrode, while the rare earth elements are −2.3 to −2. It is an element that is very obsolete as 5v, in other words, an element that is difficult to reduce.
[0032]
Therefore, in order to reduce the transition element to metal, a normal reducing gas, such as a reducing gas such as H2, CO, CH4, or the like, is introduced into the furnace to form a reducing atmosphere and heated. Is enough. During this reduction reaction, oxygen contained in the transition metal oxide powder is gradually removed in the form of H2O or CO. The heating temperature in this case is set in the range of 300 to 900 ° C. Reduction of transition metal oxides is unlikely to occur at temperatures lower than this range, and reduction occurs at temperatures higher than this range, but oxide particles cause particle growth and segregation due to high temperatures and deviate from the desired particle size. It is. Therefore, the heating temperature is more preferably in the range of 400 to 800 ° C.
[0033]
The rare earth element oxide component in the metal oxide cannot be reduced by heating in the reducing gas atmosphere described above. The method of reducing the rare earth element is not limited, but it can be achieved by mixing and heating a metal of an element having a lower reduction potential than the target rare earth element. For example, as an alkali metal, Li is -3.04, Na is -2.71, K is -2.93 v, Rb is 2.98 v, Cs is -2.92 v, and among alkaline earth metals, Mg is -2. 372v, Ca has a reduction potential of -2.87v, Sr is -2.89v, Ba has a reduction potential of -2.912v, and is mixed with the metal oxide and heated in an inert gas. Rare earth elements can be reduced to metals. The use of metallic calcium is most suitable from the viewpoint of handling safety and cost.
[0034]
The application of calcium as a reducing agent has been put to practical use for rare earth cobalt magnets by applying an alloy powder manufacturing method called a reduction diffusion method. It is most preferable in the present invention to apply this reduction diffusion method. That is, by adding metal calcium or calcium hydroxide to a powder in a mixed state of a fine metal and a rare earth element oxide obtained by reducing a transition metal element obtained by reduction with a reducing gas to a metal state, an inert gas By heating in an atmosphere or vacuum, the rare earth oxide is brought into contact with the calcium melt or its vapor, and the rare earth oxide is reduced to a metal. By this reduction reaction, an alloy block of a rare earth element and a transition metal element can be obtained.
[0035]
The alkali metal and alkaline earth metal reducing agents described above are used in the form of particles or powders. From the viewpoint of cost, granular metal calcium having a particle size of 4 mesh or less is particularly suitable. These reducing agents contain reaction equivalents (the stoichiometric amount necessary to reduce the rare earth oxide, and if the transition metal is used in the form of an oxide, it contains the amount necessary to reduce this. 1.1 to 3.0 times, preferably 1.5 to 2.0 times the amount.
[0036]
Naturally, the reduction with the reducing agent can also reduce the transition metal element. Therefore, there is no case where the transition metal oxide cannot be directly reduced with a reducing agent such as Ca without reducing the reducing gas. However, in that case, the required amount of Ca becomes excessive, and not only the particles are coarsened by the heat generated during the reduction reaction by Ca, but in the worst case, there is a risk that the product is scattered in the furnace due to an explosive reaction. . Therefore, it is preferable to metalize most of the transition metal before reduction of the rare earth element by reduction diffusion. Therefore, it is desirable that the oxygen removal rate of the transition metal before the reduction diffusion step is 40% or more. This is because, in order to remove oxygen exceeding 40%, a large amount of reducing agent is required in the next step, which is not economical, and it becomes impossible to obtain an alloy powder having a dispersed shape. is there. Here, the oxygen removal rate is a percentage of the amount of oxygen removed by reduction with respect to the total amount of oxygen present in the oxide of the transition metal.
[0037]
In the present invention, a disintegration accelerator can be used together with the reducing agent as necessary. This disintegration accelerator is appropriately used for promoting the disintegration and granulation of the product in the wet treatment described later, such as calcium chloride disclosed in JP-A-63-105909. Examples include alkaline earth metal salts and calcium oxide. These decay accelerators are used in a proportion of 1 to 30% by weight, in particular 5 to 30% by weight, based on the rare earth oxide used as the rare earth source.
[0038]
In the present invention, the raw material powder described above, a reducing agent, and a disintegration promoter used as necessary are mixed, and the mixture is reduced by heating in an inert atmosphere other than nitrogen, for example, argon gas. . The heat treatment temperature for the reduction is preferably 700 to 1200 ° C., particularly 800 to 1100 ° C., and the heat treatment time is not particularly limited, but in order to perform the reduction reaction uniformly, It can be performed in a time range of 10 minutes to 10 hours, and more preferably in a range of 10 minutes to 2 hours. The reason why the reduction-diffusion reaction can be performed in such a short time is due to the high mixing level of the raw materials according to the method of the present invention. By this reduction reaction, a porous massive rare earth-transition metal alloy is obtained.
[0039]
At this time, the reaction product is a mixture of by-produced CaO, unreacted excess calcium, and product alloy powder, and is a sintered lump state in which these are combined. Therefore, this product mixture is then poured into cooling water to separate CaO and metallic calcium from the alloy powder as a Ca (OH) 2 suspension. Further, residual Ca (OH) 2 is removed by washing the alloy powder with acetic acid or hydrochloric acid. When the porous massive rare earth-transition metal alloy of the product is thrown into water, the composite mixture is collapsed by the oxidation of metallic calcium with water and the hydration reaction of by-product CaO, That is, pulverization proceeds.
[0040]
After stirring the slurry produced by the collapse, the hydroxide such as the upper alkali metal is removed by decantation, and the hydroxide is obtained from the obtained alloy powder by repeating the water injection-stirring-decantation operation. Can be removed. Further, the partially remaining hydroxide is completely removed by acid washing with an acid such as acetic acid or hydrochloric acid at pH 3-6, preferably pH 4-5. After completion of such wet processing, for example, after washing with water, washing with an organic solvent such as alcohol or acetone, dehydration, and vacuum drying, a rare earth-transition metal alloy powder is produced.
[0041]
The above-described method is the basic constitution of the present invention, and (1) a rare earth-transition metal alloy powder can be obtained. By applying this method, (2) a rare earth-transition metal-boron system, 3) A rare earth-transition metal-nitrogen alloy powder can be obtained. That is, the present invention can be applied to any alloy that basically includes a rare earth element-transition metal having the constitution (1).
[0042]
In order to obtain the rare earth-transition metal-boron alloy of (2), a stoichiometrically necessary amount of B for obtaining a target composition is obtained after a firing step for obtaining a rare earth element-transition element metal oxide. It is possible to sufficiently mix (boron) with the metal oxide, perform the reduction with the above-described reducing gas, and subsequently perform the reduction diffusion with the reducing agent. Alternatively, once reduction with a reducing gas is performed and the transition metal oxide is sufficiently reduced, a stoichiometric amount of B (boron) is mixed, and then reduction diffusion is performed to obtain a rare earth-transition metal-boron. A system alloy can be obtained. Any of these can be obtained, but the former method is more preferable. That is, B (boron) contains about 1% of oxygen. By mixing this before the reducing step with the reducing gas, oxygen contained in this B is removed, and in the next step This is because the reduction diffusion reaction is easily performed.
[0043]
In order to obtain the rare earth-transition metal-nitrogen based alloy powder of (3), basically, after the reduction reaction by reduction diffusion is completed, nitrogen gas or heating is continued in the same furnace before proceeding to the decay process. By introducing a compound gas capable of being decomposed and supplying nitrogen, nitriding can be performed. Since the rare earth-transition metal alloy is obtained as a porous mass in the reduction diffusion step, heat treatment can be immediately performed in a nitrogen atmosphere without pulverization, whereby nitriding is performed uniformly, and the rare earth-transition metal- A nitrogen alloy is obtained. This nitriding treatment is performed by lowering the temperature from the heating temperature range for reduction to a temperature of 300 to 600 ° C., particularly 400 to 550 ° C., and replacing the atmosphere with a nitrogen atmosphere within this temperature range. For example, if the nitriding temperature is less than 300 ° C., the diffusion of nitrogen into the rare earth-transition metal alloy, which is the reaction product obtained in the above process, becomes insufficient, and nitriding is performed uniformly and effectively. It becomes difficult. Further, when the nitriding temperature exceeds 600 ° C., the rare earth-transition metal alloy is decomposed into a rare earth-nitrogen compound and a transition metal such as α-iron, so that the magnetic properties of the obtained alloy powder are remarkably deteriorated. Produce. The heat treatment time is set to such an extent that nitriding is sufficiently uniformly performed, but this time is generally about 2 to 20 hours.
[0044]
【Example】
Examples of the present invention will be described below on the basis of examples of producing Sm—Fe—N alloy powder, which is a permanent magnet material.
[0045]
[Example 1]
<1. Precipitation reaction>
513.4 g of anhydrous samarium chloride SmCl3 and 2757.6 g of anhydrous iron chloride FeCl3 were weighed and simultaneously poured into 10 liters of ion-exchanged water, and completely dissolved while stirring in a reactor to obtain a metal liquid. While continuing to stir the reactor, 5.1 kg of a 15 wt% caustic soda solution is gently put into it. After confirming that the pH of the solution is 10 or more, when the stirring is stopped and the mixture is allowed to stand, the product precipitates at the bottom of the container.
[0046]
<2. Filtration washing>
The precipitated product is taken on filter paper and sucked while supplying ion exchange water from the top. This decantation is continued until the electrical conductivity of the filtrate falls below 50 μS / m. The precipitate cake obtained after washing and suction filtration is dried in an oven at 80 ° C.
[0047]
<3. Air firing>
The dried cake is placed in an alumina crucible and baked in an atmosphere of 1000 ° C. for 5 hours.
[0048]
<4. Particle size adjustment>
The fired product is loosened by hand and then pulverized with a hammer mill. As for the particle size of this powder, the average particle size by a Fisher sub-sieving sizer (FSSS) was 1.2 μm.
[0049]
<5. Hydrogen reduction>
The pulverized powder was filled in a steel tray, placed in a tubular furnace, and subjected to heat treatment at 700 ° C. for 10 hours while flowing 100% pure hydrogen at 20 liters / minute. The resulting black powder had an oxygen concentration of 7.0 wt%.
[0050]
<6. Reduction diffusion reaction>
1000 g of black powder obtained in the previous step and 350.7 g of granular Ca are mixed, put in a steel tray, and set in an argon gas atmosphere furnace. After evacuating the inside of the furnace, it is heated at 1050 ° C. for 0.5 hour while passing argon gas. The heating is then stopped and subsequently cooled to 450 ° C. in argon gas and thereafter kept constant at this temperature. Then, after evacuating the inside of the furnace again, nitrogen gas is introduced. After heating for 5 hours while passing nitrogen gas at a pressure higher than atmospheric pressure, the heating is stopped and the mixture is allowed to cool.
[0051]
<7. Washing>
The obtained reaction product is put into 5 liters of ion-exchanged water, whereby the reaction product is immediately destroyed and separation of the alloy powder and the Ca component starts. Stirring in water, standing, and removal of the supernatant liquid are repeated 5 times, and finally, it is washed in 5 liters of a 2 wt% aqueous acetic acid solution to complete the separation of the Ca component. This is vacuum dried to obtain Sm2Fe17N3 alloy powder.
[0052]
<8. Characteristic evaluation>
The obtained powder had good dispersibility and had a spherical shape even when observed with an electron microscope. The average particle size of the powder was 2.5 μm as measured by FSSS. The magnetic properties of the powder were Br13.5KG and iHc16.2KOe. The concentration of oxygen contained in the powder was 0.2 wt%, and segregation of Sm and Fe could not be confirmed by cross-sectional observation with EPMA. Further, according to the X-ray diffraction using Cu—Kα as a radiation source, nothing other than the main phase was observed, and in particular α-Fe, which is a pure iron component, could not be found.
[0053]
[Example 2]
<1. Precipitation reaction>
Pour 30 liters of pure water into the reaction tank, add 520 g of 97% H2SO4, charge and dissolve 484.8 g of Sm2O3, and add 25% aqueous ammonia to adjust the pH to near neutral. To this aqueous solution, 5200 g of FeSO4 · 7H2O was added and completely dissolved to obtain a metal solution. In another tank, a carbonate ion solution was prepared by mixing 1224 liters of pure water with 2524 g of ammonium bicarbonate and 1738 g of 25% ammonia water. While stirring the reaction tank, a carbonate ion solution was gradually added, and ammonia water was added so that the final pH after addition of the whole amount was 8.0 ± 0.5. When stirring is stopped and allowed to stand, the product precipitates at the bottom of the container.
[0054]
<2. Filtration washing>
The precipitated product is taken on filter paper and sucked while supplying ion exchange water from the top. This decantation is continued until the electrical conductivity of the filtrate falls below 50 μS / m. The precipitate cake obtained after washing and suction filtration is dried in an oven at 80 ° C.
[0055]
<3. Air firing>
The dried cake is placed in an alumina crucible and baked in an atmosphere at 1100 ° C. for 3 hours.
[0056]
<4. Particle size adjustment>
The fired product is loosened by hand and then pulverized with a hammer mill. As for the particle size of this powder, the average particle size by a Fisher sub-sieve sizer (FSSS) was 1.3 μm.
[0057]
<5. Hydrogen reduction>
The pulverized powder was filled in a steel tray, placed in a tubular furnace, and subjected to heat treatment at 700 ° C. for 10 hours while flowing 100% pure hydrogen at 20 liters / minute. The black powder obtained had an oxygen concentration of 7.2 wt%.
[0058]
<6. Reduction diffusion reaction>
1000 g of black powder obtained in the previous step and 350.7 g of granular Ca are mixed, put in a steel tray, and set in an argon gas atmosphere furnace. After evacuating the inside of the furnace, it is heated at 1000 ° C. for 1 hour while passing argon gas. The heating is then stopped and subsequently cooled to 450 ° C. in argon gas and thereafter kept constant at this temperature. Then, after evacuating the inside of the furnace again, nitrogen gas is introduced. After heating for 5 hours while passing nitrogen gas at a pressure higher than atmospheric pressure, the heating is stopped and the mixture is allowed to cool.
[0059]
<7. Washing>
The obtained reaction product is put into 5 liters of ion-exchanged water, whereby the reaction product is immediately destroyed and separation of the alloy powder and the Ca component starts. Stirring in water, standing, and removal of the supernatant liquid are repeated 5 times, and finally, it is washed in 5 liters of a 2 wt% aqueous acetic acid solution to complete separation of the Ca component. This is vacuum dried to obtain Sm2Fe17N3 alloy powder.
[0060]
<8. Characteristic evaluation>
The obtained powder had good dispersibility and had a spherical shape even when observed with an electron microscope. The average particle size of the powder was 2.7 μm as measured by FSSS. The magnetic properties of the powder were Br13.7KG and iHc15.8kOe. The concentration of oxygen contained in the powder was 0.25 wt%, and segregation of Sm and Fe could not be confirmed by cross-sectional observation with EPMA. Further, according to X-ray diffraction using Cu—Kα as a radiation source, nothing was observed other than the Sm—Fe alloy as the main phase, and in particular, no traces of α-Fe as a pure iron component were found.
[0061]
[Example 3]
<1. Precipitation reaction>
Weigh 513.4g of samarium nitrate hexahydrate Sm (NO3) 3 · 6H2O and 3432.3g of iron nitrate nonahydrate Fe (NO3) 3 · 9H2O and add them simultaneously to 10 liters of ion-exchanged water while stirring. To do. After confirming complete dissolution, 2992.5 g of urea (NH 2) 2 CO is added while stirring is continued. The liquid temperature is raised to 80 ° C while stirring is continued. At this time, urea is hydrolyzed into ammonia and carbon dioxide, and the metal is precipitated by a homogeneous reaction.
[0062]
<2. Filtration washing>
The precipitated product is taken on filter paper and sucked while supplying ion exchange water from the top. This operation is continued until the specific resistance of the filtrate falls below 50 μS / m. The washed cake is dried in a dryer at 80 ° C.
[0063]
<3. Air firing>
The dried cake is placed in an alumina crucible and baked in an atmosphere at 1100 ° C. for 3 hours.
[0064]
<4. Particle size adjustment>
The fired product is loosened by hand and then pulverized with a hammer mill. The particle size of this powder was 1.3 microns with a Fischer sub-sieve sizer.
[0065]
<5. Hydrogen reduction>
The pulverized powder was placed in a steel tray and placed in a tubular furnace in which 100% hydrogen was circulated at a rate of 20 liters / minute, and subjected to heat treatment at 700 ° C. for 10 hours. The black powder obtained had an oxygen concentration of 7.2 wt%.
[0066]
<6. Reduction diffusion reaction>
1000 g of the black powder obtained in the previous step and 350.7 g of granular Ca having a particle size of 6 mm or less are mixed, placed in a steel tray, and set in an inert gas atmosphere furnace. After evacuating the inside of the furnace, it is heated at 1000 ° C. for 1 hour while passing argon gas. The heating is then stopped and subsequently cooled to 450 ° C. in argon gas and thereafter kept constant at this temperature. Then, after evacuating the inside of the furnace again, nitrogen gas is introduced. After heating for 5 hours while passing nitrogen gas at a pressure higher than atmospheric pressure, the heating is stopped and the mixture is allowed to cool.
[0067]
<7. Washing>
The obtained reaction product is put into 5 liters of ion-exchanged water, whereby the reaction product immediately disintegrates and separation of the alloy powder and the Ca component starts. Stirring in water, standing, and removal of the supernatant liquid are repeated 5 times, and finally, it is washed in 5 liters of a 2 wt% aqueous acetic acid solution to complete separation of the Ca component. This is vacuum dried to obtain Sm2Fe17N3 alloy powder.
[0068]
<8. Characteristics>
The obtained powder had good dispersibility and had a spherical shape even when observed with an electron microscope. The particle size of the powder was 2.8 microns with a Fisher sub-sieve sizer. The magnetic properties of the powder were Br13.8KG and iHc14.6KOe. The concentration of oxygen contained in the powder was 0.25 wt%, and segregation of Sm and Fe could not be confirmed by cross-sectional observation with EPMA. Further, according to the X-ray diffraction using Cu—Kα as a radiation source, nothing was observed other than the Sm—Fe alloy which is the main phase, and in particular, no trace of α-Fe which is a pure iron component was found.
[0069]
[Comparative Example 1]
Metal Sm and metal Fe were melted at an atomic ratio of 2 to 17. The melt was poured into a water-cooled copper mold to obtain an Sm2Fe17 alloy. The obtained ingot was coarsely pulverized with a jaw crusher and then subjected to heat treatment at 1100 ° C. for 40 hours in argon for the purpose of homogenization. The obtained alloy was pulverized by a ball mill of steel balls for 2 hours. Further, this powder was heat-treated at 100% nitrogen and 450 ° C. for 5 hours. The obtained powder was in an agglomerated state with poor dispersibility, and had an angular shape even when observed with an electron microscope. The average particle size according to the FSSS method was 2.5 μm. The magnetic properties of the powder were Br13.3 kG and iHc 8.2 kOe. The concentration of oxygen contained in the powder was 0.6 wt%, and segregation of Sm and Fe could be confirmed by cross-sectional observation with EPMA. Further, according to X-ray diffraction using Cu—Kα as a radiation source, a clear peak due to α-Fe was observed.
[0070]
【effect】
As described above, according to the present invention, the following effects can be obtained.
[0071]
Since the elements constituting the alloy powder are already homogeneously mixed at the raw material stage, it is easy to obtain a homogeneous alloy. Therefore, it is possible to draw out the physical properties specific to the material.
[0072]
The method of making an ingot of rare earth elements and fiber metal by a normal melting method and pulverizing the ingot often requires heat treatment for several tens of hours in order to obtain a homogeneous alloy. Is about several hours. By shortening the heat treatment time, a powdered product can be easily obtained.
[0073]
Furthermore, the particle shape of the precipitate particles obtained in the precipitation process is inherited by the alloy powder of the final product, and by controlling the shape of the precipitate particles, it becomes possible to obtain a dispersed alloy powder with a uniform particle shape. As a result, a magnetic material with high magnetic performance can be obtained.

Claims (2)

A step of depositing a precipitate obtained by reacting at least one cation of a rare earth element with at least one cation selected from Fe, Co, and Ni with a substance that forms an insoluble salt with the cation. ,
Calcination of the precipitate to obtain a metal oxide;
Heating the metal oxide in a reducing gas atmosphere;
A step of heating in the reducing gas atmosphere and then mixing and reducing calcium to obtain a porous mass product;
Nitriding the porous mass product,
After the nitriding treatment, washing with water and acid washing,
For producing rare earth-transition metal- nitrogen based alloy powders. The method for producing a rare earth-transition metal- nitrogen alloy powder according to claim 1 , wherein the reducing gas is hydrogen .