EP1079950A1

EP1079950A1 - Sinter-active metal and alloy powders for powder metallurgy applications and methods for their production and their use

Info

Publication number: EP1079950A1
Application number: EP99923562A
Authority: EP
Inventors: Bernd Mende; Gerhard Gille; Benno Gries; Peter Aulich; Jörg MÜNCHOW
Original assignee: HC Starck GmbH
Current assignee: HC Starck GmbH
Priority date: 1998-05-20
Filing date: 1999-05-08
Publication date: 2001-03-07
Anticipated expiration: 2019-05-08
Also published as: EP1079950B1; CN1301205A; JP2002515543A; KR20010052366A; DE19822663A1; JP4257690B2; DE59906598D1; US6554885B1; ATE246976T1; CA2332889C; JP2009001908A; AU4039399A; CN1254339C; CA2332889A1; WO1999059755A1; KR100543834B1

Abstract

A process is described for the production of metal powder and alloy powders containing at least one of the metals iron, copper, tin, cobalt or nickel, by mixing aqueous metal salt solutions with an aqueous carboxylic acid solution, separating the precipitation product from the mother liquor and reducing the precipitation product to the metal.

Description

Sintered metal and alloy powders for powder metallurgical applications and processes for their production and their use

The present invention relates to metal powder consisting of one or more of the elements Fe, Ni, Co, Cu, Sn and possible additions of Al, Cr, Mn, Mo and W, a process for their preparation and their use.

Alloy powders have diverse applications for the production of sintered materials by powder metallurgy. The main feature of powder metallurgy is that corresponding powdered alloy or metal powder is pressed and then sintered at an elevated temperature. This method has been introduced on an industrial scale for the production of complicated molded parts that can otherwise only be produced with a high degree of elaborate finishing. The sintering can be carried out as solid phase sintering or to form a liquid phase, e.g. with hard or heavy metals. A very important application of alloy and pure metal powders are tools for metal, stone and wood processing. In these cases, it is a matter of two-phase materials, whereby the hardness carriers (e.g. carbides or diamonds) are embedded in a metallic matrix, which ensures the required toughness properties of these

Composites is responsible. The hard metals produced in this way (in the case of carbides or carbonitrides) or diamond tools (in the case of diamonds) are of considerable economic importance.

The element cobalt plays a special role because it is used as a metallic matrix

Diamond and carbide tools have some special properties. Because it wets tungsten carbide and diamonds particularly well, it is traditionally preferred for both types of tools. The use of cobalt for the metallic binder phase in composite materials based on tungsten carbide or diamond achieves particularly good adhesion of the hardness carrier in the metallic binder phase. What is important here is the fact that in the case of cobalt the tendency for the formation of carbides of the type Co3W3C ("eta phases"), which lead to embrittlement in hard metals, is less pronounced than, for example, in the case of iron. Co also attacks diamonds less than, for example, iron, which easily forms Fe ₃ C. For these technical reasons, cobalt is traditionally used in the carbide and diamond tool industry.

In the production of hard metals, cobalt metal powders 0.8 to 2 μm FSSS (ASTM B330) are generally used, which together with the hard materials, pressing aids and a grinding fluid are subjected to mixed grinding in air gates or ball mills, which contain hard metal balls as grinding media become. The suspension obtained is then separated from the grinding media, spray-dried, and the granules obtained are pressed into molds. The subsequent liquid phase sintering at temperatures above the melting point of the W-Co-C eutectic results in dense sintered bodies (hard metals). An important property of the hard metals produced in this way is their strength

Porosity is weakened. Industrial hard metals have a porosity better than or equal to A02B00C00 according to ASTM B276 (or DIN ISO 4505). The A-porosity is the microporosity, while the B-porosity is the macroporosity. In contrast to hard materials, cobalt metal powders are ductile and are not crushed during mixed grinding, but plastically deformed or the existing agglomerates disassembled. If the cobalt metal powder used contains large, sintered, large agglomerates, they are transferred into the spray granules in deformed form and result in A and B porosity in the sintered hard metal, often associated with local enrichment of the binder phase.

Diamond tools as a second important application group contain sintered parts (segments) as cutting or grinding active components, which consist mainly of diamonds, embedded in a metallic binder phase, mainly cobalt. In addition, hard materials or other metal powders are optionally added to match the wear behavior of the bond on the diamond and the materials to be machined. For the production of segments Metal powder, diamonds and possibly hard material powder mixed, optionally granulated and densely sintered in hot presses at elevated pressure and temperature. The requirements placed on the binder metal powder in addition to the necessary chemical purity are: good compactibility, the highest possible sintering activity, one that is tailored to the diamond and the medium to be processed

Hardness, adjusted by the grain size and the tendency to coarsen the structure during sintering, as well as little attack on the diamond which is metastable at sintering temperature (graphitization).

In general, the porosity decreases with increasing sintering temperature, i.e. the density of the

Sinterstücks approaches its theoretical value. For reasons of strength, the sintering temperature is therefore chosen to be as high as possible. On the other hand, the hardness of the metallic matrix drops again above an optimal temperature because the structure becomes coarser. In addition, it should be noted that at higher temperatures there is an increased attack on the diamond. For these reasons, binder powder is preferred for segments that already reach their theoretical density at the lowest possible sintering temperatures and that can be easily compacted.

The limited availability of cobalt, strong price fluctuations, environmental aspects and the desire for technical improvement have led to numerous activities to replace cobalt in the hard metal and diamond tool industry.

There are already a number of proposals to replace cobalt as a binder metal at least partially by iron and / or nickel or their alloys (metal,

40: 133-140 (1986); Int. J. of Refractory Metals & Hard Materials 15 (1997) 139-149).

A disadvantage of the production of diamond tools using metal powders of the individual elements and bronze powders is that the metallic

Binding after sintering is very inhomogeneous, since the sintering temperature and time at Homogenization is not enough. In addition, when using ferrous metal powders, high pressing forces occur, which wear out the pressing tools and lead to low strengths of the green compacts (eg edge breakouts). This is also due to the cubic, body-centered grating type of iron, which has fewer sliding planes than the cubic, face-centering types of cobalt and

Nickel or copper metal powder. In addition, the finer carbonyl iron powders available contain high amounts of carbon, which can lead to a loss of strength in the segment. Atomized metal powders or alloys do not have sufficient sintering activity, so that the temperatures that are acceptable for diamonds are still insufficiently compacted.

When producing hard metals using carbonyl iron powders there are problems with the binder distribution (A and / or B porosity). This can be compensated for by more intensive grinding. However, this leads to an undesirable broadening of the grain size distribution.

Accordingly, there are also a number of proposals for metallic alloy powder by precipitation, in some cases. in the presence of organic phases, and subsequent reduction (WO 92/18 656, WO 96/04 088, WO 97/21 844).

The object of the invention is to provide metal and alloy powders containing at least one of the metals iron, copper, tin, cobalt or nickel which meet the requirements mentioned for binder metals for hard metals and diamond tools. The metal and alloy powders according to the invention can be modified by doping with the elements Al, Cr, Mn, Mo and / or W in a minor amount and adapted to special requirements.

The invention firstly relates to a method for producing the metal and

Alloy powder by mixing aqueous metal salt solutions with a carboxylic acid solution, separating the precipitate from the mother liquor and

Reduction of the precipitate to the metal, which is characterized in that the carboxylic acid is used overstoichiometrically and as a concentrated aqueous solution.

After separation from the mother liquor, the precipitate is preferably washed with water and dried.

The precipitation product is preferably reduced in a hydrogen-containing atmosphere at temperatures between 400 and 600 ° C. The reduction can take place in the indirectly heated rotary kiln or in the push-through furnace with little bed cover. Other options for carrying out the reduction are readily known to the person skilled in the art, such as in the deck oven or in the fluidized bed.

According to a preferred embodiment of the invention, the dried precipitation product is calcined at temperatures between 250 and 500 ° C. before the reduction in an oxygen-containing atmosphere. The calcination, on the one hand, has the effect that the precipitation product consisting of polycrystalline particles or agglomerates is comminuted by the gases released during the decomposition of the carboxylic acid residue by decrepitation, so that a larger surface area is available for the subsequent gas phase reaction (reduction) and a finer end product is obtained.

On the other hand, calcination in an oxygen-containing atmosphere results in the formation of a metal or alloy powder which has a significantly reduced porosity compared to direct reduction. When the (mixed) metal carboxylic acid salt is converted to the metal or alloy powder, there is a considerable reduction in the volume of the particles, which leads to the inclusion of pores. Through the intermediate calcination step in an oxygen-containing atmosphere, the (mixed) metal carboxylic acid salt is first converted into the (mixed) metal oxide and annealed, so that pre-compression takes place with the healing of lattice defects. In the subsequent reduction in a hydrogen-containing atmosphere, only the volume shrinkage from oxide to metal has to be overcome. The intermediate calcination step leads to a gradual volume shrinkage achieved, each with structural stabilization of the crystals after each shrinkage stage.

Suitable carboxylic acids are aliphatic or aromatic, saturated or unsaturated mono- or dicarboxylic acids, in particular those with 1 to 8 carbon atoms. Because of their reducing effect, formic acid, oxalic acid, acrylic acid and crotonic acid are preferred, and because of their availability, formic and oxalic acid in particular. Oxalic acid is particularly preferably used. The excess of reducing carboxylic acids prevents the formation of Fe (III) ions, which would lead to problems during the precipitation.

The carboxylic acid is preferably used in a 1.1- to 1.6-fold stoichiometric excess, based on the metals. A 1.2- to 1.5-fold excess is particularly preferred.

According to a further preferred embodiment of the invention, the carboxylic acid solution is used as a suspension which contains undissolved carboxylic acid in suspension. The preferably used carboxylic acid suspension contains a deposit of undissolved carboxylic acid, from which the carboxylic acid withdrawn by precipitation of the solution is replaced, so that a high concentration of carboxylic acid is maintained in the mother liquor throughout the precipitation reaction. The concentration of dissolved carboxylic acid in the mother liquor should preferably be at least 20% of the saturation concentration of the carboxylic acid in water at the end of the precipitation reaction. At the end of the precipitation reaction, the concentration of dissolved carboxylic acid in the mother liquor should particularly preferably still be 25 to 50% of the saturation concentration of the carboxylic acid in water.

A chloride solution is preferably used as the metal salt solution. The concentration of the metal salt solution is preferably about 1.6 to 2.5 mol per liter. The metal salt solution preferably has a content of 10 to 90% by weight of iron, based on the total metal content and at least one further of the elements Copper, tin, nickel or cobalt. The content of iron in the metal salt solution is particularly preferably at least 20% by weight, more preferably at least 25% by weight, very particularly preferably at least 50% by weight, but less than 80% by weight, very particularly preferably less than 60 wt .-%, each based on the total metal content.

The metal salt solutions further preferably contain 10 to 70% by weight, particularly preferably up to 45% by weight, of cobalt, based on the total metal content. The nickel content of the metal salt solution is preferably 0 to 50% by weight, particularly preferably up to 16% by weight.

Copper and / or tin can be used in amounts of up to 30% by weight, preferably up to 10% by weight, based on the total metal content. According to the particularly preferred embodiment of the process according to the invention, the metal salt solution is gradually added to the carboxylic acid suspension in the

That the content of dissolved carboxylic acid in the mother liquor during the supply of the metal salt solution does not fall below 50% of the solubility of carboxylic acid in water. The metal salt solution is particularly preferably added gradually such that the concentration of dissolved carboxylic acid does not fall below 80% of the solubility in until the suspended carboxylic acid has dissolved

Water falls below. The rate of addition of the metal salt solution to the carboxylic acid suspension thus takes place in such a way that the withdrawal of carboxylic acid from the mother liquor, including concentration reduction, is largely compensated for by dilution with the water supplied with the metal salt solution by dissolving undissolved, suspended carboxylic acid.

With regard to the precipitation of the metal salts, a concentrated carboxylic acid solution has "activity 1", and only a half-concentrated carboxylic acid solution has "activity 0.5". According to the invention, the activity of the mother liquor should accordingly preferably not fall below 0.8 during the addition of the metal salt solution. For example, the solubility of the oxalic acid which is preferably used in water is approximately 1 mol per liter of water (room temperature), corresponding to 126 g of oxalic acid (2 molecules of water of crystallization). According to the preferred method according to the invention, the oxalic acid should be introduced as an aqueous suspension which contains 2.3 to 4.5 mol of oxalic acid per liter of water. This suspension contains about 1.3 to 3.5 moles of undissolved oxalic acid per liter of water. After the metal salt solution has been introduced and the precipitation has ended, the content of oxalic acid in the mother liquor should still be 20 to 55 g / l of water. During the introduction of the metal salt solution into the oxalic acid suspension, the oxalic acid consumed for the precipitation is constantly replaced by the dissolution of suspended oxalic acid. The mother liquor is constantly stirred to homogenize it. According to the preferred embodiment, the metal salt solution is added gradually such that the oxalic acid concentration in the mother liquor does not drop below 75 g, particularly preferably not less than 100 g, per liter of mother liquor during the addition. This has the effect that a sufficiently high supersaturation is constantly achieved during the addition of the metal salt solution

Nucleation, i.e. is sufficient to generate further precipitation particles. This on the one hand ensures a high nucleation rate, which leads to correspondingly small particle sizes, and on the other hand largely prevents agglomeration of the particles due to dissolution due to the low metal ion concentration present in the mother liquor.

The high carboxylic acid concentration, which is preferred according to the invention, during the precipitation also has the effect that the precipitation product has the same composition as the metal salt solution in terms of the relative contents of metals, i.e. that there is a homogeneous precipitation product with respect to its composition and thus alloy metal powder.

The invention further relates to metal and alloy powders which contain at least one of the elements iron, copper, tin, nickel or cobalt and which can optionally be doped in a minor amount by one or more of the elements Al, Cr, Mn, Mo, W. , and the average grain size according to ASTM B330 (FSSS) from 0.5 to 5 μ, preferably below 3 μm. The alloy powders according to the invention are characterized in that they have no fracture surfaces produced by grinding. They are available with this grain size immediately after reduction. Preferred metal or alloy particles according to the invention have a very low carbon content of less than

0.04% by weight, preferably less than 0.01% by weight. This is due to the temperature treatment carried out between precipitation and reduction in an oxygen-containing atmosphere, in which the organic carbon present after the precipitation is removed. Metal or alloy powders preferred according to the invention furthermore have an oxygen content of less than 1% by weight, preferably less than 0.5% by weight. The preferred composition of the alloy powders according to the invention corresponds to the preferred relative metal contents of the metal salt solutions used, as stated above. The metal and alloy powders according to the invention are outstandingly suitable as binder metals for hard metals or diamond tools. They are also suitable for the powder metallurgical production of components.

The metal and alloy powders according to the invention show higher sintering activity, more complete alloy formation and better wetting with the hardness carrier in the production of hard metals due to their finely dispersed distribution and thus lead to non-porous hard metals.

The metal and alloy powders according to the invention are also distinguished by the fact that they can be sintered to very dense sintered bodies even at a comparatively low temperature. The invention accordingly also relates

Metal and alloy powders which, after sintering at a temperature of 650 ° C and exposure to a pressure of 35 MPa for 3 minutes, form a sintered body which has more than 96%, preferably more than 97%, of the theoretical material density. Particularly preferred alloy powders according to the invention already achieve more than 97% of the theoretical material density at a sintering temperature of 620 ° C. In this context, “theoretical material density” is to be understood as the density of an alloy with a corresponding composition produced by melting in a vacuum.

The invention is explained in more detail below with the aid of the attached examples 1 to 7.

Examples 1 to 4

In each case 6.3 l of a metal chloride solution containing 75 g / 1 Fe, 15 g / 1 Ni and 10 g / 1 Co were stirred into a suspension of 1954 g oxalic acid (1.4 times the stoichiometric amount based on the metal salts ) gradually metered in in the amount of water specified in Table 1. After the precipitation had ended, the mixture was stirred for a further 30 minutes, then the precipitate was filtered off and washed with water. The oxalate was dried at 105 ° C. to constant weight. The particle sizes (FSSS) of the dried mixed oxalate are given in Table 1. The mixed oxalate was then calcined in the muffle furnace at 300 ° C. for 3 hours and then reduced to the alloy metal powder in a push-through furnace at 500 ° C. under hydrogen.

27 g of the mixed metal powder were ground with 273 g of WC (grade DS80 with 0.15% VC, manufacturer HCSt, Goslar) with the addition of 0.3 g of soot in the attritor under hexane. After the grinding balls had been separated off and the ground material had been dried, a green body was produced and sintered as follows with a pressure of 1500 kg / cm ² : 20 ° C./min to 1100 ° C., holding at this temperature for 60 minutes, further heating at a rate of 20 ° C / min to 1400 ° C, 45 min hold at this temperature, cooling to 1100 ° C, 60 min hold at this temperature and cooling to room temperature. The sintered body had the properties given in Table 1.

Table 1

* clear solution ** uneven particle size distribution Example 5

There were 39 1 of a metal chloride solution with 50 g / 1 Fe, 42.3 g / 1 Co and 7.7 g / 1 Ni at room temperature with constant stirring over a period of 30 min in a suspension of 12.877 kg oxalic acid in 45 1 water metered in and then stirred for a further 60 min. It was then filtered, washed and the oxalate was dried to constant weight at 110 ° C. The oxalate was calcined in the muffle furnace at 300 ° C for 3 h and the oxide thus produced was subsequently reduced to metal powder in a row in three successive heating zones at 480/500/530 ° C in 130 min under hydrogen (dew point 10 ° C). An FS SS value of 0.71 μm, a physical density of 7.76 g / cm ³ and a bulk density of 0.24 g / cm ^{3 were} measured on the metal powder; the oxygen content was determined to be 0.71%.

A hard metal test was carried out on this metal powder under identical conditions as in Examples 1 to 4. A density of 14.54 g / cm ³ , a Vickers hardness HV ₃₀ = 1817 kg / mm ² and a porosity <A02B00C00 according to ASTM B276 (no visible microporosity under the light microscope at 200 × magnification) were measured on the test body.

Example 6

The oxalate precipitation was carried out as in Example 5, but a chloride solution with 42.7 g / 1 Co and 56.3 g / 1 Fe was used.

The calcination in the muffle furnace was carried out at 250 ° C. The three-stage reduction under hydrogen was carried out at 520/550/570 ° C.

25 g each of this Fe-Co alloy powder were sintered in a graphite matrix in a vacuum (hot press from Dr. Fritsch, type TSP) at a pressure of 35 MPa over a pressing time of 3 min at different temperatures. The results shown in Table 2 were achieved.

Table 2

*) Theoretical density = mean value of the densities of Co and Fe according to their percentage = 8.37 g / cm ³

Example 7

An iron-cobalt-copper oxalate was precipitated, washed and dried analogously to Example 1, using a metal chloride solution containing about 45 g / 1 Fe, 45 g / 1 Co and 10 g / 1 Cu.

Part of the mixed metal oxalate obtained was transferred directly into the hydrogen stream

Reduced for 6 hours at 520 ° C (Charge A). Another part of the material was first treated under atmospheric air for 3 hours at 300 ° C and then reduced over 130 minutes at 520 ° C in a hydrogen stream (Batch B).

The metal powders had the properties shown in Table 3. Table 3

Hot press tests as in Example 6 were carried out on the metal powders. The results are given in Table 4 (HBR = Rockwell hardness B, SD = sintered density g / cm ³ ,% TD =% of the theoretical density):

Table 4

Claims

claims

1. A process for the preparation of metal and alloy powders containing at least one of the metals iron, copper, tin, cobalt or nickel, by mixing aqueous metal salt solutions with an aqueous carboxylic acid solution, separating the precipitate from the mother liquor and reducing the precipitate to the metal.

2. The method according to claim 1, characterized in that the precipitation product is subjected to a thermal decomposition at 200 to 1000 ° C in an oxygen-containing atmosphere prior to the reduction to the metallic alloy powder.

3. The method according to claim 1 or 2, characterized in that a saturated aqueous carboxylic acid solution is used.

4. The method according to claim 3, characterized in that the aqueous carboxylic acid solution contains solid carboxylic acid in such an amount that the mother liquor is still at least 10% saturated after completion of the precipitation, based on metal salt-free aqueous solution.

5. The method according to any one of claims 1 to 4, characterized in that the metal salt solution is introduced into an aqueous carboxylic acid solution.

6. The method according to any one of claims 1 to 4, characterized in that aqueous metal salt solution and carboxylic acid are continuously introduced into a precipitation reactor and continuously withdrawing a mother liquor containing the precipitation product.

7. Metal or alloy powder containing at least one of the elements

Iron, copper, tin, nickel or cobalt, with an average grain size according to ASTM B 330 of less than 7 μm.

8. metal or alloy powder according to claim 7 with a carbon content of less than 0.04 wt .-%.

9. Metal or Alloy powder according to claim 7 or 8, which after sintering at a pressure of 35 MPa at 650 ° C for 3 minutes a sintered body with a density of at least 96% of the theoretical physical density of the

Metal or the alloy forms.

10. Use of the metal or alloy powder according to one of claims 1 to 9 as a binder metal for hard metals or diamond tools or as an alloy powder for powder metallurgical production of components.