US3846126A - Powder metallurgy production of high performance alloys - Google Patents

Powder metallurgy production of high performance alloys Download PDF

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Publication number
US3846126A
US3846126A US00323502A US32350273A US3846126A US 3846126 A US3846126 A US 3846126A US 00323502 A US00323502 A US 00323502A US 32350273 A US32350273 A US 32350273A US 3846126 A US3846126 A US 3846126A
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powder
alloy
binder
mesh
alloy powder
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US00323502A
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H Rogers
E Foley
D Dreyer
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Stoody Co
Deloro Stellite LP
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Cabot Corp
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Priority to US00323502A priority Critical patent/US3846126A/en
Priority to ZA739585A priority patent/ZA739585B/en
Priority to DE2365046A priority patent/DE2365046C2/en
Priority to IN09/CAL/74A priority patent/IN140276B/en
Priority to AR251846A priority patent/AR199602A1/en
Priority to BR74159A priority patent/BR7400159D0/en
Priority to PL1974168106A priority patent/PL88512B1/en
Priority to IT67094/74A priority patent/IT1009104B/en
Priority to CA190,070A priority patent/CA1031603A/en
Priority to NL7400498A priority patent/NL7400498A/xx
Priority to CH45874A priority patent/CH587091A5/xx
Priority to BE139794A priority patent/BE809726A/en
Priority to AU64462/74A priority patent/AU480246B2/en
Priority to FR7401195A priority patent/FR2213826B1/fr
Priority to ES422274A priority patent/ES422274A1/en
Priority to AT74274A priority patent/ATA27474A/en
Priority to SE7400430A priority patent/SE401110B/en
Priority to LU69150A priority patent/LU69150A1/xx
Priority to JP49007494A priority patent/JPS5756523B2/ja
Priority to HUCA360A priority patent/HU168185B/hu
Priority to CS74250A priority patent/CS216185B2/en
Priority to DD176014A priority patent/DD112725A5/xx
Priority to GB180174A priority patent/GB1457661A/en
Priority to US05/434,091 priority patent/US3988524A/en
Publication of US3846126A publication Critical patent/US3846126A/en
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Priority to US05/826,362 priority patent/US4129444A/en
Priority to JP56050035A priority patent/JPS5933654B2/en
Assigned to STOODY COMPANY, A CORP. OF DE reassignment STOODY COMPANY, A CORP. OF DE ASSIGNMENT OF ASSIGNORS INTEREST. SUBJECT TO CONDITIONS RECITED Assignors: CABOT CORPORATION, A CORP. OF DE
Assigned to STOODY DELORO STELLITE, INC. reassignment STOODY DELORO STELLITE, INC. CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). EFFECTIVE JULY 1, 1986 Assignors: STOODY COMPANY A CORP. OF DE
Assigned to WELLS FARGO BANK, N.A. reassignment WELLS FARGO BANK, N.A. SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: STOODY DELORO STELLITE, INC.
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Assigned to SOCIETY NATIONAL BANK, INDIANA reassignment SOCIETY NATIONAL BANK, INDIANA SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HAYNES INTERNATIONAL, INC.
Assigned to HAYNES INTERNATIONAL, INC. reassignment HAYNES INTERNATIONAL, INC. ACKNOWLEDGEMENT, RELEASE AND TERMINATION AGREEMENT Assignors: SOCIETY BANK, INDIANA, N.A.
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/04Making non-ferrous alloys by powder metallurgy
    • C22C1/0433Nickel- or cobalt-based alloys
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/10Metallic powder containing lubricating or binding agents; Metallic powder containing organic material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F1/00Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
    • B22F1/14Treatment of metallic powder
    • B22F1/148Agglomerating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F3/00Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
    • B22F3/12Both compacting and sintering

Definitions

  • a powder metallurgy process suitable for high performance alloys difficult to compact and/ or sinter involves coating the particles with a solid organic binder by dry blending the alloy powder with particles of the binder, mixing the blended particles with a solvent for the binder to produce a plastic mass, consolidating this mass to discrete bodies of an intermediate density, drying the bodies, crushing them and screening the resulting agglomerates, pressing them into green compacts, and sintering those compacts.
  • Some or all of the starting powder may be ground to smaller particle size. As fine grinding is always accompanied by oxidation of the powder, which is detrimental to sinterability, the grinding is adjusted to produce particles of a limited average size range.
  • This invention relates to the production by powder metallurgy of articles of hard metal alloys. It is more particularly concerned wth production by this method of articles of high performance metal alloys.
  • the alloys with which this invention is concerned are high performance cobalt-base, nickel-base, and iron-base chromium-containing alloys resistant to wear, heat and corrosion. These alloys either are not workable or are worked with difficulty, and are commonly produced as castings, which may be ground or machined where necessary. Many small articles made from high performance alloys, such as thread guides for textile mills, valve seat inserts, and the like, are tedious and expensive to cast in the quantities that are required. Attempts have been made to produce such articles by powder metallurgical process, such as by slip casting or pressing the articles to shape from fine powders, and then sintering them. However, such processes, which have proved satisfactory and economical for many alloys, have turned out to be difiicult and expensive to adapt to alloys as hard as the high performance alloys here concerned.
  • the powder particles should be of spherical configuration and of a random size distribution over a rather wide range of sizes to provide optimum packing density and so facilitate subsequent densification.
  • US. Pat. 3,639,179 of Steven Reichman et al. of Feb. 1, 1972, Method of Making Large Grain Sized Superalloys the patentees recommended a size range of about 150 microns to about microns. We have found, however, that a number of high performance alloy powders when compacted in this way can be sintered only in a very narrow range of temperatures, or in some cases not at all.
  • the density of the sintered article is generally required to be of cast density or better, all compacts shrink from about 25 to as much as 40% or more during sintering, Where the sintered compact must meet close dimensional tolerances the compacts are constrained during sintering.
  • the green compacts are slipped over mandrels and sintered in that position. If the cohesion between the powder particles is insufficient the compacts will crack.
  • the average particle size required for effective compacting in the worst case, was found to be less than about 5 microns, and the grinding time necessary for such powder was measured in days. This, of course, considerably increased its cost. Moreover, the greatly increased surface area of the very fine powder and the length of time required for its grinding facilitated oxidation of the powder so that, in spite of all precautions, its oxygen content was much greater than that of atomized powder. This high oxygen content is undesirable for several reasons, one overriding reason being that it narrows the sintering range of the powder. Thus, the sinterable powders were not compactible for many of the alloys, and the compactible powders were, effectively, not sinterable.
  • Our process to be described is adapted to utilize the full size range of atomized melts of many high performance alloys if maximum density in the resulting article is not desired. It is also adapted to high performance alloys which by conventional processes are unsinterable or marginally sinterable.
  • compositions of a number of alloys for which our process is suitable are listed in the accompanying Table.
  • Noun-Balance includes incidental impurities.
  • the alloy powder which we employ is preferably produced by the atomization of a melt of the desired composition.
  • This melt is heated to a temperature of 200 F. or so above its fusion temperature in a crucible.
  • this melting is carried out in vacuum or under a blanket of inert gas such as argon.
  • the melt is then poured into a preheated refractory tundish which is formed with a small diameter nozzle in the bottom through which the stream of metal flows into an atomizing chamber.
  • the stream emerging from the nozzle is broken up into fine particles by a high-pressure jet of inert gas, or of water, which makes contact with the molten stream just below the nozzle.
  • the particles or droplets are almost instantaneously quenched by the atomizing fluid and fall into a reservoir in the bottom of the atomizing chamber. Only the fraction is used which passes through a mesh screen. These particles are approximately spherical in shape and about 25% to of the particles are 325 I mesh. A 325 mesh screen will pass particles the greatest dimension of which is 44 microns.
  • polyvinyl alcohol as a binder for our powder, but other solid binders which are known to the art are employed. Examples are camphor, methyl alcohol, paradichlorobenzene, chloroacetic acid, naphthalene, benzoic acid, phthalic anhydride, glycerine, Acrowax C, which is a proprietary compound, the ethylene oxide polymers sold as Carbowax, synthetic gums such as acrylamide, and metal stearates.
  • the solvent for the binder must be appropriately chosen. Water is satisfactory for water-soluble binders.
  • the blending of the powder and binder particles is accomplished in any suitable mixing apparatus.
  • the amount of binder is not critical, and a few percent by weight is sufficient. Extrusion of the plastic or putty-like blend of particles, binder and solvent is the most convenient way of consolidating the plastic mixture into agglomerates, but other methods, such as roll briquetting, may be employed.
  • the extrusions are then dried, crushed in a roller crusher, hammer mill or the like, and screened.
  • the l00 mesh fraction of crushed extruded binder powder is largely fines. From about 60 to 80% of the particles are 325 mesh with corresponding apparent densities of about 2.0 to 3.3 grams per cc. Both the percentage of fines and the compacting pressure can be as low as 20 tons per sq. inch or as high as 70 tons per sq. inch, the density of the green compacts being higher at higher compaction pressures. At a compaction pressure of 20 tons per sq. inch, compact density is about 56 to 58% of cast density, and at 70 tons per sq. inch it is 70 to 72% of cast density.
  • the desired density of the finished article is obtained by sintering the compact in vacuum or reducing atmosphere at a temperature between the solidus temperature and liquidus temperature of the alloy. Sintering can be completed in about an hour, but if the time is extended to two or at most three hours, the temperature can be reduced somewhat without impairing the properties of the article. Compacts properly sintered have densities of 98% or better of cast density.
  • Our process also contemplates grinding, when necessary, of part or all of the powder particles resulting from the atomization of a melt as above described.
  • relatively coarse atomized powder such as -30 mesh by ball miling, impact milling, attriting, vibrating milling, or other known process so as to convert it to particles more than 98% of which are 325 mesh and process those particles in the way described above to produce sintered articles having improved properties.
  • the milling vehicle which we prefer to use is methanol, the mill is preferably evacuated to minimize oxidation of the charge, and, in the case of ball milling, the balls charged are made of a wear-resistant alloy of a composition compatible with the product being produced.
  • Milling time ranges from about 8 to 36 hours and the average particle size of the 325 mesh product ranges from about 30 microns to as low as 9 microns, depending on milling conditions.
  • the charge is dumped from the mill and the powder allowed to settle.
  • the alcohol is decanted and the sludge is vacuum filtered.
  • the powder filter cake is allowed to dry under vacuum or in air, and is then crushed to 60 mesh agglomerates of bindered particles.
  • the 30 mesh atomized powder milled to an average particle size of about microns can be sintered to 95% density or better within a temperature range of about to This range is broad enough for commercial operation.
  • the oxygen content of the milled powder is about 0.44%. It is interesting to find that the addition of a relatively minor amount of a fine fraction of the atomized particles to milled powder appreciably impairs its sinterability.
  • a charge of 30 +270 mesh atomized powder of No. 7 alloy was ground in a ball mill for 25 hours to an average particle size of about 10 microns. This material was mixed with 270 mesh atomized powder in amount representing 30% by weight of the aggregate. The average particle size of this aggregate was 23.5 microns.
  • Compacts of the aggregate did not sinter as well as compacts of -30 +270 mesh atomized powder milled in a ball mill for 18 hours to an average particle size of 15 microns.
  • the first mentioned powder had to be sintered at a temperature of 2300 F. for better than an hour to achieve 95 density. Sintering at 2310 F. for an hour resulted in an article density of 98.25%.
  • the second mentioned powder achieved a compact density of 95 after one hour of sintering at 2280 F. and 98% after one hour at 2290 F.
  • EXAMPLE I The 325 mesh fraction of atomized powder of Alloy No. 3 of the Table was dry blended in a mixer with particles of a binder, preferably 100 mesh polyvinyl alcohol, in amounts of 2% to 3% by weight.
  • the powder particles used had an average particle size of about 30 microns.
  • enough warm water was added to form a plastic mixture of the powder and binder.
  • This mixture was then extruded into cylinders or roundels of about two inches long and one-half inch in diameter under pressure sufficient to consolidate the mixture to a density of about 60% of cast density.
  • the roundels were dried, then crushed in a roller crusher, hammer mill, or the like, and the crushed material was screened to -100 mesh.
  • the -l00 mesh agglomerates of blended alloy powder particles were formed under pressure of about tons per sq. inch into green compacts of the desired shape, which had sufficient strength to withstand further processing.
  • the green compacts were then sintered for 1 to 3 hours at a temperature of between 2260 F. and 2325 F.
  • the binder volatilized during sintering and the sintered articles had a density of 97% to 99% of cast density.
  • EXAMPLE II Inert gas atomized powder of Alloy No. 7, a nickelbase alloy, was screened through a 30 mesh screen. One hundred pounds of the screened powder were charged into a 28" long ball mill along with 13 gallons of methanol and about 800 pounds of Haynes Stellite Alloy No. 3 balls. The mill was evacuated and run at approximately 80% of critical speed (54 r.p.m.) for 10 hours. The average particle size of the resulting powder was about 17.5 microns. About 98% of the powder was 325 mesh.
  • the powder was removed from the mill, filtered, dried, and dry blended with 2% by weight of 100 mesh polyvinyl alcohol particles, and 1% by weight of Acrowax C, mixed with water to form a putty-like mass, extruded into roundels, dried, crushed, charged into a die, pressed and removed from the die.
  • the coherent green compacts were placed in a sintering furnace and sintered at a temperature between 2210 F. and 2230 F. for a period of time of 1 to 3 hours.
  • the articles resulting had a density of 98% to 99% of cast density and Rockwell C scale hardness of 41 to 44.
  • EXAMPLE IV Inert gas atomized particles of Alloy No. 8, which is an iron-base alloy, were screened through a 325 mesh screen. The particles passing through the screen were then mixed with a binder as described in Example I, except that the binder was 3% polyvinyl alcohol, and further processed as there described into green compacts. These compacts held their shape, and were transferred to a sintering furnace and sintered at a temperature between 2150" F. and 2170 F. to articles having a density of 97% of cast density.
  • EXAMPLE V Inert gas atomized particles of Alloy No. 8 of 30 mesh size were ground in a ball mill for 24 hours to particles of an average particle size of about 9 microns. These particles were then blended with 3% by weight of polyvinyl alcohol particles and 1% by weight of particles of Acrowax C and further processed as is described in Example I into coherent green compacts. Those compacts were sintered at a temperature between 2140 F. and 2170 F. to articles having a density of 97% of cast density.
  • the vehicle chosen for the ball milling has some effect on the sintering process. While we would prefer to use water, we find that its use results in a measurable increase in the oxygen content of the sintered article and a narrowing of the temperature range for sintering. Where the oxygen content of the alloy is critical or where the sintering range is restricted we use a solvent other than water. In the case of No. 7 alloy, for example, made from powder of about 18 microns average size, the increase in oxygen content of the alloy arising from the use of water as a vehicle is about 0.43%. We prefer to use methanol as a vehicle, which brings about an increase in oxygen content of only about 0.12%. Other organic solvents that may be used as vehicles are ketones, aromatic hydrocarbons and methane series compounds.
  • the decomposition of organic binders increases the carbon content of the sintered article in amounts between about 0.1% and 0.2%.
  • this increase can be significant, and in such cases we added to the powder small amounts of an oxide of a metal which is reduced by carbon at the sintering temperature.
  • Cobalt oxide is suitable for Alloy No. 3 and is preferred by us.
  • nickel oxide or oxides of other metals compatible with the alloy composition may be used.
  • alloys consisting of a matrix of Alloy No. 2 having particles of tungsten carbide dispersed therein in amounts from about 25% to about 60% by weight.
  • the tungsten carbide powder is added to the alloy powder and mechanically mixed therewith.
  • the powder mix is then blended with a suitable binder and processed from that point on in the same way as is described in the examples above set out.
  • the screen sizes are ASTM screen sizes. Average particle sizes were determined by Sharples Micromerograph.

Abstract

1. THE PROCESS OF MAKING A COHERENT GREEN COMPACT WHICH HODS ITS SHAPED DURING SINTERING FROM PRE-ALLOYED COMMINUTED POWDER OF A HIGH PERFORMANCE METAL ALLOY WHICH CANNOT BE PRESSURE COMPACTED UNDER PRESSURES UP TO 70 TONS PER SQUARE INCH UNLESS ITS AVERAGE PARTICLE SIZE IS NOT GREATER THAN ABOUT 5 MICRONS, COMPRISING PROCESSING THE ALLOY POWDER TO AN AVERAGE PARTICLE SIZE BETWEEN ABOUT 9 AND ABOUT 30 MICRONS, MIXING THE ALLOY POWDER WITH A DRY, FINELY DIVIDED ORGANIC BINDER IN AMOUNTS NOT GREATER THAN ABOUT 5% BY WEIGHT OF THE ALLOY POWDER SO AS TO OBTAIN A UNIFORM DISPERSION OF BINDER IN THE ALLOY POWDER, THEN ADDING A SOLVENT FOR THE BINDER IN AMOUNT SUFFICIENT TO FORM A PLASTIC MIXTURE WITH THE ALLOY POWDER AND BINDER, THEN CONSOLIDATING THE PLASTIC MIXTURE TO A BULK DENSITY INTERMEDIATE THAT OF THE POWDER AND THAT OF THE CAST ALLOY, THEN DRYING THE CONSOLIDATED MIXTURE TO EVAPORATE THE SOLVENT, THEN CRUSHING THE CONSOLIDATED MIXTURE TO DISCRETE AGGLOMERATES OF PRE-ALLOYED POWDER PARTICLES TO PROVIDES A SUBSTANTIAL FRACTION OF -100 MESH PARTICLES AT LEAST ABOUT HALF OF THE -100 MESH FRACTION OF WHICH ARE-325 MESH, THEN FILLING A DIE OF THE DESIRED SHAPED WITH THOSE AGGLOMERATES, THEN COMPACTING THE AGGLOMERATES IN THE DIE UNDER PRESSURE TO AT LEAST ABOUT 50% OF THE CAST DENSITY OF THE ALLOY SO AS TO PRODUCE A COHERENT GREEN COMPACT, AND THEN REMOVING THE COMPACT FROM THE DIE.

Description

3,846,126 POWDER METALLURGY PRODUCTION OF HIGH PERFORMANCE ALLOYS Edward M. Foley, Russiaville, and Dennis G. Dreyer and Herbert E. Rogers, Jr., Kokomo, Ind., assignors to Cabot Corporation No Drawing. Filed Jan. 15, 1973, Ser. No. 323,502
Int. Cl. B22f 1/00 US. Cl. 75211 12 Claims ABSTRACT OF THE DISCLOSURE A powder metallurgy process suitable for high performance alloys difficult to compact and/ or sinter involves coating the particles with a solid organic binder by dry blending the alloy powder with particles of the binder, mixing the blended particles with a solvent for the binder to produce a plastic mass, consolidating this mass to discrete bodies of an intermediate density, drying the bodies, crushing them and screening the resulting agglomerates, pressing them into green compacts, and sintering those compacts.
Some or all of the starting powder may be ground to smaller particle size. As fine grinding is always accompanied by oxidation of the powder, which is detrimental to sinterability, the grinding is adjusted to produce particles of a limited average size range.
This invention relates to the production by powder metallurgy of articles of hard metal alloys. It is more particularly concerned wth production by this method of articles of high performance metal alloys.
The alloys with which this invention is concerned are high performance cobalt-base, nickel-base, and iron-base chromium-containing alloys resistant to wear, heat and corrosion. These alloys either are not workable or are worked with difficulty, and are commonly produced as castings, which may be ground or machined where necessary. Many small articles made from high performance alloys, such as thread guides for textile mills, valve seat inserts, and the like, are tedious and expensive to cast in the quantities that are required. Attempts have been made to produce such articles by powder metallurgical process, such as by slip casting or pressing the articles to shape from fine powders, and then sintering them. However, such processes, which have proved satisfactory and economical for many alloys, have turned out to be difiicult and expensive to adapt to alloys as hard as the high performance alloys here concerned.
One difliculty is that of achieving the desired high density in the finished article. It has been generally considered that the powder particles should be of spherical configuration and of a random size distribution over a rather wide range of sizes to provide optimum packing density and so facilitate subsequent densification. In US. Pat. 3,639,179 of Steven Reichman et al. of Feb. 1, 1972, Method of Making Large Grain Sized Superalloys, the patentees recommended a size range of about 150 microns to about microns. We have found, however, that a number of high performance alloy powders when compacted in this way can be sintered only in a very narrow range of temperatures, or in some cases not at all.
Experiments have indicated that the sintering of metal powders, in general, can be improved by decreasing the particl size of the powder to --325 mesh or less, If this is done by screening the powder through a fine screen only a fraction of the powder is used, which is not economical. In powder atomized from an alloy melt, which is a type of powder widely used in powder metallurgy, only 25% to 35% of the powder is 325 mesh, for example. We attempted to salvage overscreen powder by grinding it to United States Patent 0 3,846,126 Patented Nov. 5, 1974 ICC finer size and found that sinterable powder of the high performance alloys here concerned could be obtained. In many instances, however, this powder was deficient in coherence under pressure, unless it was ground to a considerably smaller particle size than was necessary for sintering.
In the production of articles from iron powder or the powder of ordinary alloys it is conventional to compress the powder into green compacts, so-called, in the shape of the desired article, and then transfer those compacts to a furnace where they are sintered. Those compacts must keep their shape until the particles are bonded by the sintering operation. The stresses which green compacts must withstand depend, among other considerations, on the shape of the compact and its dimensional tolerances. The bulk density of compacts ranges from about 50% of cast density to about 70% where high compacting pressures are employed. As the density of the sintered article is generally required to be of cast density or better, all compacts shrink from about 25 to as much as 40% or more during sintering, Where the sintered compact must meet close dimensional tolerances the compacts are constrained during sintering. In the manufacture of valve seat inserts which must be made to close inside diameter tolerances, for example, the green compacts are slipped over mandrels and sintered in that position. If the cohesion between the powder particles is insufficient the compacts will crack.
The average particle size required for effective compacting, in the worst case, was found to be less than about 5 microns, and the grinding time necessary for such powder was measured in days. This, of course, considerably increased its cost. Moreover, the greatly increased surface area of the very fine powder and the length of time required for its grinding facilitated oxidation of the powder so that, in spite of all precautions, its oxygen content was much greater than that of atomized powder. This high oxygen content is undesirable for several reasons, one overriding reason being that it narrows the sintering range of the powder. Thus, the sinterable powders were not compactible for many of the alloys, and the compactible powders were, effectively, not sinterable.
It is an object of our invention, therefore, to provide a process of producing articles of high performance alloys by powder metallurgy which economically utilizes atomized powders. Another object is to provide such a process which broadens the range of sintering temperatures. Another object is to provide such -a process which tolerates the use of particles of larger screen size than prior known processes. It is still another object to provide a process adaptable to high performance alloys not sinterable by presently known powder metallurgy process. Other objects of our invention will appear from the description thereof which follows.
We have found that compactability of high performance alloy powders is greatly improved by coating the particles with a binder in a way to be described, and that the coarse fraction of the powder can be reduced to a particle size suit-able for sintering in a relatively brief grinding operation which does not increase the oxygen content of the powder to unacceptable levels.
Our process to be described is adapted to utilize the full size range of atomized melts of many high performance alloys if maximum density in the resulting article is not desired. It is also adapted to high performance alloys which by conventional processes are unsinterable or marginally sinterable. It comprehends the milling of a relatively coarse fraction of an atomized melt, or the entire product, so as to reduce the particles to a size which is not accompanied by unacceptable oxidation, the dry blending of this powder with a binder, and the mixing of that blend with a solvent for the binder to produce a plastic mass, the consolidation of this mass to discrete bodies of an intermediate density, the drying and crushing of those bodies and screening of the resulting agglomerates to about 100 mesh size, the pressing of the agglomerates into green compacts which hold their shape, the transfer of those compacts to a furnace, and the sintering of those compacts.
Compositions of a number of alloys for which our process is suitable are listed in the accompanying Table.
COMPOSITIONS OF TYPICAL ALLOYS IN WEIGHT PERCENT Alloying elements Alloy Co Ni Si Fe Mn Cr Mo W C V B P S 3 Bal. 9.5 1.0 2.0 1 0 24.5 7.0 0.15 11.5 ..26.5 8.0 0.55
5 Bal. 2.5 1.0 3.0 1.0 31.0 16.0 2.20 34.0..---.. 19.0 2.70
6 Bal. 2.0 1.0 2.5 1028.0 0.8 17.0 1.70 5.0 32. 20.0 2.20
7 9.0 Bal. 11.5 0.75 25.0 9.0 9.0 1.30 1.0
8 0.5 Bal. 0.5 15.5 14.5 2.90 165 1.5 18.5 17.5 3.40 2 10 Maximum.
Noun-Balance includes incidental impurities.
The alloy powder which we employ is preferably produced by the atomization of a melt of the desired composition. This melt is heated to a temperature of 200 F. or so above its fusion temperature in a crucible. Preferably, this melting is carried out in vacuum or under a blanket of inert gas such as argon. The melt is then poured into a preheated refractory tundish which is formed with a small diameter nozzle in the bottom through which the stream of metal flows into an atomizing chamber. The stream emerging from the nozzle is broken up into fine particles by a high-pressure jet of inert gas, or of water, which makes contact with the molten stream just below the nozzle. The particles or droplets are almost instantaneously quenched by the atomizing fluid and fall into a reservoir in the bottom of the atomizing chamber. Only the fraction is used which passes through a mesh screen. These particles are approximately spherical in shape and about 25% to of the particles are 325 I mesh. A 325 mesh screen will pass particles the greatest dimension of which is 44 microns.
We prefer to use polyvinyl alcohol as a binder for our powder, but other solid binders which are known to the art are employed. Examples are camphor, methyl alcohol, paradichlorobenzene, chloroacetic acid, naphthalene, benzoic acid, phthalic anhydride, glycerine, Acrowax C, which is a proprietary compound, the ethylene oxide polymers sold as Carbowax, synthetic gums such as acrylamide, and metal stearates. The solvent for the binder must be appropriately chosen. Water is satisfactory for water-soluble binders.
The blending of the powder and binder particles is accomplished in any suitable mixing apparatus. The amount of binder is not critical, and a few percent by weight is sufficient. Extrusion of the plastic or putty-like blend of particles, binder and solvent is the most convenient way of consolidating the plastic mixture into agglomerates, but other methods, such as roll briquetting, may be employed.
The extrusions are then dried, crushed in a roller crusher, hammer mill or the like, and screened. The l00 mesh fraction of crushed extruded binder powder is largely fines. From about 60 to 80% of the particles are 325 mesh with corresponding apparent densities of about 2.0 to 3.3 grams per cc. Both the percentage of fines and the compacting pressure can be as low as 20 tons per sq. inch or as high as 70 tons per sq. inch, the density of the green compacts being higher at higher compaction pressures. At a compaction pressure of 20 tons per sq. inch, compact density is about 56 to 58% of cast density, and at 70 tons per sq. inch it is 70 to 72% of cast density.
The desired density of the finished article is obtained by sintering the compact in vacuum or reducing atmosphere at a temperature between the solidus temperature and liquidus temperature of the alloy. Sintering can be completed in about an hour, but if the time is extended to two or at most three hours, the temperature can be reduced somewhat without impairing the properties of the article. Compacts properly sintered have densities of 98% or better of cast density.
Our process also contemplates grinding, when necessary, of part or all of the powder particles resulting from the atomization of a melt as above described. We grind relatively coarse atomized powder, such as -30 mesh by ball miling, impact milling, attriting, vibrating milling, or other known process so as to convert it to particles more than 98% of which are 325 mesh and process those particles in the way described above to produce sintered articles having improved properties. The milling vehicle which we prefer to use is methanol, the mill is preferably evacuated to minimize oxidation of the charge, and, in the case of ball milling, the balls charged are made of a wear-resistant alloy of a composition compatible with the product being produced. Milling time ranges from about 8 to 36 hours and the average particle size of the 325 mesh product ranges from about 30 microns to as low as 9 microns, depending on milling conditions. After milling, the charge is dumped from the mill and the powder allowed to settle. The alcohol is decanted and the sludge is vacuum filtered. The powder filter cake is allowed to dry under vacuum or in air, and is then crushed to 60 mesh agglomerates of bindered particles.
Compacts of 30 mesh atomized powder of Alloy N0. 7 cannot be sintered. The -325 mesh fraction of this powder, which has an average particle size 'of about 31 microns, can be sintered, although the temperature range for density is rather narrow. As has been mentioned, however, the 325 mesh fraction of the atomized powder represents only about 25% to 35% of the powder.
The 30 mesh atomized powder milled to an average particle size of about microns can be sintered to 95% density or better within a temperature range of about to This range is broad enough for commercial operation. The oxygen content of the milled powder is about 0.44%. It is interesting to find that the addition of a relatively minor amount of a fine fraction of the atomized particles to milled powder appreciably impairs its sinterability. In another run a charge of 30 +270 mesh atomized powder of No. 7 alloy was ground in a ball mill for 25 hours to an average particle size of about 10 microns. This material was mixed with 270 mesh atomized powder in amount representing 30% by weight of the aggregate. The average particle size of this aggregate was 23.5 microns. Compacts of the aggregate did not sinter as well as compacts of -30 +270 mesh atomized powder milled in a ball mill for 18 hours to an average particle size of 15 microns. The first mentioned powder had to be sintered at a temperature of 2300 F. for better than an hour to achieve 95 density. Sintering at 2310 F. for an hour resulted in an article density of 98.25%. The second mentioned powder achieved a compact density of 95 after one hour of sintering at 2280 F. and 98% after one hour at 2290 F.
EXAMPLE I The 325 mesh fraction of atomized powder of Alloy No. 3 of the Table was dry blended in a mixer with particles of a binder, preferably 100 mesh polyvinyl alcohol, in amounts of 2% to 3% by weight. The powder particles used had an average particle size of about 30 microns. Then enough warm water was added to form a plastic mixture of the powder and binder. This mixture was then extruded into cylinders or roundels of about two inches long and one-half inch in diameter under pressure sufficient to consolidate the mixture to a density of about 60% of cast density. The roundels were dried, then crushed in a roller crusher, hammer mill, or the like, and the crushed material was screened to -100 mesh. The -l00 mesh agglomerates of blended alloy powder particles were formed under pressure of about tons per sq. inch into green compacts of the desired shape, which had sufficient strength to withstand further processing. The green compacts were then sintered for 1 to 3 hours at a temperature of between 2260 F. and 2325 F. The binder volatilized during sintering and the sintered articles had a density of 97% to 99% of cast density.
EXAMPLE II Inert gas atomized powder of Alloy No. 7, a nickelbase alloy, was screened through a 30 mesh screen. One hundred pounds of the screened powder were charged into a 28" long ball mill along with 13 gallons of methanol and about 800 pounds of Haynes Stellite Alloy No. 3 balls. The mill was evacuated and run at approximately 80% of critical speed (54 r.p.m.) for 10 hours. The average particle size of the resulting powder was about 17.5 microns. About 98% of the powder was 325 mesh. The powder was removed from the mill, filtered, dried, and dry blended with 2% by weight of 100 mesh polyvinyl alcohol particles, and 1% by weight of Acrowax C, mixed with water to form a putty-like mass, extruded into roundels, dried, crushed, charged into a die, pressed and removed from the die. The coherent green compacts were placed in a sintering furnace and sintered at a temperature between 2210 F. and 2230 F. for a period of time of 1 to 3 hours. The articles resulting had a density of 98% to 99% of cast density and Rockwell C scale hardness of 41 to 44.
EXAMPLE III Inert gas atomized powder of Alloy No. 6, which is a cobalt-base alloy, was milled as is described in Example II except for a time of 36 hours to powder having an aver- =*'Registered Trademark of Cabot Corporation.
age particle size of 11.5 microns. This powder was then processed as described above, except that 3% polyvinyl alcohol plus 1% Acrowax C constituted the binder, into coherent compacts, which were transferred to a sintering furnace and sintered at a temperature between 2140" F. and 2160 F. The finished articles had a density of 96 to 98% of cast density.
EXAMPLE IV Inert gas atomized particles of Alloy No. 8, which is an iron-base alloy, were screened through a 325 mesh screen. The particles passing through the screen were then mixed with a binder as described in Example I, except that the binder was 3% polyvinyl alcohol, and further processed as there described into green compacts. These compacts held their shape, and were transferred to a sintering furnace and sintered at a temperature between 2150" F. and 2170 F. to articles having a density of 97% of cast density.
EXAMPLE V Inert gas atomized particles of Alloy No. 8 of 30 mesh size were ground in a ball mill for 24 hours to particles of an average particle size of about 9 microns. These particles were then blended with 3% by weight of polyvinyl alcohol particles and 1% by weight of particles of Acrowax C and further processed as is described in Example I into coherent green compacts. Those compacts were sintered at a temperature between 2140 F. and 2170 F. to articles having a density of 97% of cast density.
The vehicle chosen for the ball milling has some effect on the sintering process. While we would prefer to use water, we find that its use results in a measurable increase in the oxygen content of the sintered article and a narrowing of the temperature range for sintering. Where the oxygen content of the alloy is critical or where the sintering range is restricted we use a solvent other than water. In the case of No. 7 alloy, for example, made from powder of about 18 microns average size, the increase in oxygen content of the alloy arising from the use of water as a vehicle is about 0.43%. We prefer to use methanol as a vehicle, which brings about an increase in oxygen content of only about 0.12%. Other organic solvents that may be used as vehicles are ketones, aromatic hydrocarbons and methane series compounds.
On the other hand, the decomposition of organic binders increases the carbon content of the sintered article in amounts between about 0.1% and 0.2%. In Alloy No. 3 and lower carbon high performance alloys known to the art, this increase can be significant, and in such cases we added to the powder small amounts of an oxide of a metal which is reduced by carbon at the sintering temperature. Cobalt oxide is suitable for Alloy No. 3 and is preferred by us. For other alloys, nickel oxide or oxides of other metals compatible with the alloy composition may be used.
Our process is useful in the manufacture from powder of alloys containing a dispersed phase. We have made thereby, alloys consisting of a matrix of Alloy No. 2 having particles of tungsten carbide dispersed therein in amounts from about 25% to about 60% by weight. The tungsten carbide powder is added to the alloy powder and mechanically mixed therewith. The powder mix is then blended with a suitable binder and processed from that point on in the same way as is described in the examples above set out.
In the foregoing description of the process the screen sizes are ASTM screen sizes. Average particle sizes were determined by Sharples Micromerograph.
In the foregoing specification we have described a presently preferred embodiment of this invention, however, it will be understood that this invention can be otherwise embodied within the scope of the following claims.
We claim:
1. The process of making a coherent green compact which holds its shape during sintering from pre-alloyed comminuted powder of a high performance metal alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about 5 microns, comprising processing the alloy powder to an average particle size between about 9 and about 30 microns, mixing the alloy powder with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder so as to obtain a uniform dispersion of binder in the alloy powder, then adding a solvent for the binder in amount sufiicient to form a plastic mixture with the alloy powder and binder, then consolidating the plastic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of pro-alloyed powder particles to provide a substantial fraction of 100 mesh particles at least about half of the -100 mesh fraction of which are 325 mesh, then filling a die of the desired shape with those agglomerates, then compacting the agglomerates in the die under pressure to at least about 50% of the cast density of the alloy so as to produce a coherent green compact, and then removing the compact from the die.
2. The process of claim 1 including the step of sintering the green compact at a temperature between the solidus and liquidus temperature of the alloy.
3. The process of making a coherent green compact which holds its shape during sintering from comminuted powder of a high performance metal alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about 5 microns, comprising processing the alloy powder to an average particle size between about 9 and about 30 microns, mixing the alloy powder with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder and a powdered metal oxide which is reduced by carbon at sintering temperatures so as to obtain a uniform dispersion of binder and metal oxide in the alloy powder, then adding a solvent for the binder in amount sufiicient to form a plastic mixture with the alloy powder and binder, then consolidating the plastic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of alloy powder particles at least about half of the l mesh fraction of which are 3Z5 mesh, then filling a die of the desired shape wtih those agglomerates, then compacting the agglomerates in the die under pressure to at least about 50% of the cast density of the alloy so as to produce a coherent green compact and then removing the compact from the die.
4. The process of making a coherent green compact which holds its shape during sintering from comminuted powder of a high performance metal alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about 5 microns, comprising processing the alloy powder to an average particle size between about 9 and about 30 microns, mixing the alloy powder with a powder of a substance which appears as a dispersed phase in the sintered article and with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder so as to obtain a uniform dispersion of binder in the alloy powder, then adding a solvent for the binder in amount sufiicient to form a plastic mixture with the alloy powder and binder, then consolidating the plas tic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of alloy powder particles at least about half of the 100 mesh fraction 8 of which are 325 mesh, then filling a die of the desired shape with those agglomerates, then compacting the agglomerates in the die under pressure to at least about 50% of the cast density of the alloy so as to produce a coherent green compact, and then removing the compact from the die.
5. The process of claim 1 in which the high performance metal alloy is a cobalt-base, nickel-base, or ironbase alloy.
6. The process of making a sintered article by means of a coherent green compact which holds its shape during sintering from a comminuted powder of a high performance metal alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about 5 microns, comprising producing an alloy powder by atomizing with a fluid a melt of an alloy consisting of chromium between 24.5% and 26.5%, tungsten between 7.0% and 8.0%, carbon between 0.45% and 0.55%, nickel between 9.5% and 11.5%, silicon up to 1.0%, iron up to 2.0%, manganese up to 1.0%, phosphorous not more than 0.04%, sulfur not more than 0.04%, and the balance cobalt and incidental impurities, screening the atomized powder through a 325 mesh screen, mixing the alloy powder with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder so as to obtain a uniform dispersion of binder in the alloy powder, then adding a solvent for the binder in amount sufficient to form a plastic mixture with the alloy powder and binder, then consolidating the plastic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of alloy powder particles at least about half of the l00 mesh fraction of which are 325 mesh, then filling a die of the desired shape with those agglomerates, then compacting the agglomerates in the die under pressure to at least about 50% of the cast density of the alloy so as to produce a coherent green compact, and then removing the compact from the die, and sintering the alloy at a temperature between 2260 F. and 2325 F.
7. The process of making a sintered article by means of a coherent green compact which holds its shape during sintering from a comminuted powder of a high performance alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about 5 microns, comprising producing an alloy powder by atomizing with a fluid a melt of an alloy consisting of chromium between 15.5% and 18.5%, molybdenum between 14.5% and 17.5%, carbon between 2.90% and 3.40%, vanadium between 1.65% and 2.10%, silicon between 0.5% and 1.5%, up to 0.5% manganese, and the balance iron and incidental impurities, screening the atomized powder through a 325 mesh screen, mixing the alloy powder with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder so as to obtain a uniform dispersion of binder in the alloy powder, then adding a solvent for the binder in amount sufiicient to form a plastic mixture with the alloy powder and binder, then consolidating the plastic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of alloy powder particles at least about half of the mesh fraction of which are 325 mesh, then filling a die of the desired shape with those agglomerates, then compacting the agglomerates in the die under pressure to at least about 50% of the cast density of the alloy so as to produce a coherent green compact, and then removing the compact from the die, and sintering the alloy at a, temperature between 2150 F. and 2170 F.
8. The process of making a coherent green compact which holds its shape during sintering from comminuted powder of a high performance metal alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about microns, comprising producing an alloy powder by atomizing an alloy melt with a fluid and in which at least some of the alloy powder is comminuted by grinding it to an average particle size less than about 30 microns but greater than about 9 microns, mixing the alloy powder with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder so as to obtain a uniform dispersion of binder in the alloy powder, then adding a solvent for the binder in amount sufficient to form a plastic mixture with the alloy powder and binder, then consolidating the plastic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of alloy powder particles at least about half of the 100 mesh fraction of which are 325 mesh, then filling a die of the desired shape with those agglomerates, then compacting the agglomerates in the die under pressure to at least about 50% of the cast density of the alloy so as to produce a coherent green compact, and then removing the compact from the die.
9. The process of claim 8 in which about 95% or more of the alloy powder mixed with the binder is 325 mesh.
10. The process of making a sintered article by means of a coherent green compact which holds its shape during sintering from a comminuted powder of a high performance alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about 5 microns, comprising producing an alloy which consists of chromium between 28.0% and 32.0%, tungsten between 17.0% and 20.0%, carbon between 1.70% and 2.20%, vanadium between 3.70% and 4.70%, boron between 0.7% and 1.5%, nickel between 2% and 5%, molydenum up to 0.8%, silicon up to 1.0%, iron up to 2.5%, manganese up to 1% and the balance cobalt and incidental impurities, by comminuting the alloy powder to an average particle size of about 12 microns or less mixing the alloy powder with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder so as to obtain a uniform dispersion of binder in the alloy powder, then adding a solvent for the binder in amount sufficient to form a plastic mixture with the alloy powder and binder, then consolidating the plastic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of alloy powder particles at least about half of the -100 mesh fraction of which are 325 mesh, then filling a die of the desired shape with those agglomerates, then compacting the agglomerates in the die under pressure to at least about 50% of the cast density of the alloy so as to produce a coherent green compact, and then removing the compact from the die, and then sintering the alloy at a temperature between about 2140 F. and about 2160 F.
11. The process of making a sintered article by means of a coherent green compact which holds its shape during sintering formed from a comminuted powder of a high performance alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about 5 microns, comprising producing an alloy which consists of chromium between 25.0% and 27.0%, molybdenum between 9.0% and 11.0%, tungsten between 9.0% and 11.0%, carbon between 1.30% and 1.5%, iron between 11.5% and 13.5%, phosphorus not more than 0.04%, sulfur not more than 0.3%, manganese up to 0.75%, silicon up to 1.0%, boron up to 1.0%, cobalt between 9.0% and 11.0% and the balance nickel and incidental impurities, by comminuting the alloy powder to an average particle size of about 18 microns or less, mixing the alloy powder with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder so as to obtain a uniform dispersion of binder in the alloy powder, then adding a solvent for the binder in amount sufficient to form a plastic mixture with the alloy powder and binder, then consolidating the plastic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of alloy powder particles at least about half of the 100 mesh fraction of which are 325 mesh, then filling a die of the desired shape with those agglomerates, then compacting the agglomerates in the die under pressure to at least about 50% of the cast density of the alloy so as to produce a coherent green compact, and then removing the compact from the die and then sintering the alloy at a temperature between about 2210 F. and about 2230 F.
12. The process of making a sintered article by means of a coherent green compact which hold-s its shape during sintering formed from a comminuted powder of a high performance alloy which cannot be pressure compacted under pressures up to 70 tons per square inch unless its average particle size is not greater than about 5 microns, comprising producing an alloy which consists of chromium between 15.5% and 18.5%, molybdenum between 14.5% and 17.5%, carbon between 2.90% and 3.40%, vanadium between 1.65% and 2.10%, silicon between 0.5% and 1.5 manganese up to 0.5% and the balance iron and incidental impurities, by comminuting the alloy powder to an average particle size of about 12 microns or less, mixing the alloy powder with a dry, finely divided organic binder in amounts not greater than about 5% by weight of the alloy powder so as to obtain a uniform dispersion of binder in the alloy powder, then adding a solvent for the binder in amount sufiicient to form a plastic mixture with the alloy powder and binder, then consolidating the plastic mixture to a bulk density intermediate that of the powder and that of the cast alloy, then drying the consolidated mixture to evaporate the solvent, then crushing the consolidated mixture to discrete agglomerates of alloy powder particles at least about half of the 100 mesh fraction of which are 325 mesh, then filling a die of the desired shape with those agglomerates, then compacting the agglomerates in the die under pressure to at least 50% of the cast density of the alloy so as to produce a coherent green compact, and then removing the compact from the die, and then sintering the alloy at a tem perature between about 2140 F. and about 2170 F.
References Cited UNITED STATES PATENTS 2,857,270 10/1958 Brundin --213 3,639,179 2/ 1972 Reichman et a1. 75171 3,615,381 10/1971 Hammond 75213 3,671,230 6/1972 Smythe et a1 75213 CARL D. QUARFORTH, Primary Examiner B. HUNT, Assistant Examiner US. Cl. X.'R, 75-200, 213, 221
l UNITED STATES PATENT OFFICE I CERTIFICATE OF CORRECTION Patent No. 3,846,126 Dated November 5, 1974 l t Edward M. Foley et a1.
It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shownbelow:
Column 1, line 66, "particl" should read .--particle--.
In the Table, Columns 3 and 4, Alloy 3, under element C, "0. 5" should read --0.45--.
Column 10, Claim 11, line 3, "0.3%" should read --o. o3%,-- r Y r 7 Signed end sealed this 14th day of January 1975.
(salt) Attest: v McCOY M. GIBSON: JR. 0. MARSHALL DANN Attesting Officer Commissioner of Petents FORM PO-IOSO (10-69) USCOMM-DC 60376-P69 h 11.5. GOVERNMENT PRINTING ornti mu o-ass-au.
UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3,846,126 Dated November 5, 1974 l Edward M. Foley et a1.
It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown' below:
Column l',- line 66, "particl" should read .--particle-.
In the Table, Columns 3 and 4, Alloy 3, under element C, "0..5" should read -0.45--.
Column 10, Claim 11, line 3, "0.3%" should read -0. O3%--.
Signed and sealed this 14th day of January 1975.
(sad 1;)
Attest: MccOY M. GIBSON: JR. c. MARSHALL mum Arresting Officer Conmissioner of Patents FORM PO-IOSO (10-69) USCOMNl-DC 60376-P69 w 0.5. Govsnuunrr rnlu'l'me orncz; nu o-asI-su.

Claims (1)

1. THE PROCESS OF MAKING A COHERENT GREEN COMPACT WHICH HODS ITS SHAPED DURING SINTERING FROM PRE-ALLOYED COMMINUTED POWDER OF A HIGH PERFORMANCE METAL ALLOY WHICH CANNOT BE PRESSURE COMPACTED UNDER PRESSURES UP TO 70 TONS PER SQUARE INCH UNLESS ITS AVERAGE PARTICLE SIZE IS NOT GREATER THAN ABOUT 5 MICRONS, COMPRISING PROCESSING THE ALLOY POWDER TO AN AVERAGE PARTICLE SIZE BETWEEN ABOUT 9 AND ABOUT 30 MICRONS, MIXING THE ALLOY POWDER WITH A DRY, FINELY DIVIDED ORGANIC BINDER IN AMOUNTS NOT GREATER THAN ABOUT 5% BY WEIGHT OF THE ALLOY POWDER SO AS TO OBTAIN A UNIFORM DISPERSION OF BINDER IN THE ALLOY POWDER, THEN ADDING A SOLVENT FOR THE BINDER IN AMOUNT SUFFICIENT TO FORM A PLASTIC MIXTURE WITH THE ALLOY POWDER AND BINDER, THEN CONSOLIDATING THE PLASTIC MIXTURE TO A BULK DENSITY INTERMEDIATE THAT OF THE POWDER AND THAT OF THE CAST ALLOY, THEN DRYING THE CONSOLIDATED MIXTURE TO EVAPORATE THE SOLVENT, THEN CRUSHING THE CONSOLIDATED MIXTURE TO DISCRETE AGGLOMERATES OF PRE-ALLOYED POWDER PARTICLES TO PROVIDES A SUBSTANTIAL FRACTION OF -100 MESH PARTICLES AT LEAST ABOUT HALF OF THE -100 MESH FRACTION OF WHICH ARE-325 MESH, THEN FILLING A DIE OF THE DESIRED SHAPED WITH THOSE AGGLOMERATES, THEN COMPACTING THE AGGLOMERATES IN THE DIE UNDER PRESSURE TO AT LEAST ABOUT 50% OF THE CAST DENSITY OF THE ALLOY SO AS TO PRODUCE A COHERENT GREEN COMPACT, AND THEN REMOVING THE COMPACT FROM THE DIE.
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ZA739585A ZA739585B (en) 1973-01-15 1973-12-09 Powder metallurgy production of high performance alloys
DE2365046A DE2365046C2 (en) 1973-01-15 1973-12-28 Powder metallurgical processing of high temperature materials
IN09/CAL/74A IN140276B (en) 1973-01-15 1974-01-02
AR251846A AR199602A1 (en) 1973-01-15 1974-01-08 PROCEDURE FOR PRODUCING A DENSE ARTICLE FROM A METALLIC ALLOY
BR74159A BR7400159D0 (en) 1973-01-15 1974-01-11 PROCESS TO MANUFACTURE, FROM THE POINT OF A LEAGUE, A DENSE ARTICLE
PL1974168106A PL88512B1 (en) 1973-01-15 1974-01-12 Powder metallurgy production of high performance alloys[us3846126a]
LU69150A LU69150A1 (en) 1973-01-15 1974-01-14
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CH45874A CH587091A5 (en) 1973-01-15 1974-01-14
BE139794A BE809726A (en) 1973-01-15 1974-01-14 ELABORATION OF HIGH PERFORMANCE ALLOYS FOLLOWING POWDER METALLURGY TECHNIQUES
AU64462/74A AU480246B2 (en) 1973-01-15 1974-01-14 Powder metallurgy production of high performance alloys
FR7401195A FR2213826B1 (en) 1973-01-15 1974-01-14
ES422274A ES422274A1 (en) 1973-01-15 1974-01-14 Powder metallurgy production of high performance alloys
AT74274A ATA27474A (en) 1973-01-15 1974-01-14 METHOD FOR PRODUCING SINTERED OBJECTS FROM SUPER ALLOYS
SE7400430A SE401110B (en) 1973-01-15 1974-01-14 SEE THAT FROM ALLOYING POWDER PRODUCE A TENS BODY WHICH HAS PROPERTIES EQUIVALENT TO OR SUPERIATED THOSE OF A MOLDED BODY
IT67094/74A IT1009104B (en) 1973-01-15 1974-01-14 PROCEDURE FOR THE MANUFACTURING OF ARTICLES SINTERED FROM HIGH PERFORMANCE ALLOY POWDERS
JP49007494A JPS5756523B2 (en) 1973-01-15 1974-01-14
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CA190,070A CA1031603A (en) 1973-01-15 1974-01-14 Powder metallurgy production of high performance alloys
CS74250A CS216185B2 (en) 1973-01-15 1974-01-15 Method of making the metal objects
DD176014A DD112725A5 (en) 1973-01-15 1974-01-15
GB180174A GB1457661A (en) 1973-01-15 1974-01-15 Production of articles from alloy powder
US05/434,091 US3988524A (en) 1973-01-15 1974-01-17 Powder metallurgy compacts and products of high performance alloys
US05/826,362 US4129444A (en) 1973-01-15 1977-08-22 Power metallurgy compacts and products of high performance alloys
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US3988524A (en) * 1973-01-15 1976-10-26 Cabot Corporation Powder metallurgy compacts and products of high performance alloys
US4062678A (en) * 1974-01-17 1977-12-13 Cabot Corporation Powder metallurgy compacts and products of high performance alloys
US4070184A (en) * 1976-09-24 1978-01-24 Gte Sylvania Incorporated Process for producing refractory carbide grade powder
US4121927A (en) * 1974-03-25 1978-10-24 Amsted Industries Incorporated Method of producing high carbon hard alloys
US4129444A (en) * 1973-01-15 1978-12-12 Cabot Corporation Power metallurgy compacts and products of high performance alloys
US4225345A (en) * 1978-08-08 1980-09-30 Adee James M Process for forming metal parts with less than 1 percent carbon content
US4249944A (en) * 1979-04-09 1981-02-10 Fansteel Inc. Method of making electrical contact material
US4343650A (en) * 1980-04-25 1982-08-10 Cabot Corporation Metal binder in compaction of metal powders
US4663241A (en) * 1980-09-08 1987-05-05 United Technologies Corporation Powder metal disk with selective fatigue strengthening
US4722826A (en) * 1986-09-15 1988-02-02 Inco Alloys International, Inc. Production of water atomized powder metallurgy products
US4834800A (en) * 1986-10-15 1989-05-30 Hoeganaes Corporation Iron-based powder mixtures
DE4101292A1 (en) * 1990-01-17 1991-07-18 Quebec Metal Powders Ltd DETACH-FREE METALLURGICAL POWDER MIXTURES USING A POLYVINYLPYRROLIDONE BINDING AGENT
US5298055A (en) * 1992-03-09 1994-03-29 Hoeganaes Corporation Iron-based powder mixtures containing binder-lubricant
EP0698435A1 (en) 1994-08-24 1996-02-28 Quebec Metal Powders Ltd. Powder metallurgy apparatus and process using electrostatic die wall lubrication
US5498276A (en) * 1994-09-14 1996-03-12 Hoeganaes Corporation Iron-based powder compositions containing green strengh enhancing lubricants
US6039784A (en) * 1997-03-12 2000-03-21 Hoeganaes Corporation Iron-based powder compositions containing green strength enhancing lubricants
WO2004085099A1 (en) * 2003-03-27 2004-10-07 Höganäs Ab Cobalt-based metal powder and method for producing components thereof
US20040234407A1 (en) * 2003-03-27 2004-11-25 Hoganas Ab Powder metal composition and method for producing components thereof
US20050044988A1 (en) * 2003-09-03 2005-03-03 Apex Advanced Technologies, Llc Composition for powder metallurgy
US20060198751A1 (en) * 2003-03-27 2006-09-07 Hoganas Ab, Co-based water-atomised powder composition for die compaction
US20090252636A1 (en) * 2008-04-08 2009-10-08 Christopherson Jr Denis B Powdered metal alloy composition for wear and temperature resistance applications and method of producing same
EP2436793A1 (en) * 2008-10-20 2012-04-04 H.C. Starck GmbH Metal powder
US20130306019A1 (en) * 2010-11-09 2013-11-21 Katsunori Otobe High-toughness cobalt-based alloy and engine valve coated with same
EP2857124A1 (en) 2013-10-03 2015-04-08 Kennametal Inc. Aqueous slurry for making a powder of hard material
EP2860274A2 (en) 2013-10-04 2015-04-15 Kennametal India Limited Hard material and method of making the same from an aqueous hard material milling slurry
US9162285B2 (en) 2008-04-08 2015-10-20 Federal-Mogul Corporation Powder metal compositions for wear and temperature resistance applications and method of producing same
US9624568B2 (en) 2008-04-08 2017-04-18 Federal-Mogul Corporation Thermal spray applications using iron based alloy powder
US20170291220A1 (en) * 2016-04-06 2017-10-12 Seiko Epson Corporation Metal powder for powder metallurgy, compound, granulated powder, sintered body, and heat resistant component
WO2021067036A1 (en) * 2019-09-30 2021-04-08 The Penn State Research Foundation Cold sintering process for densification and sintering of powdered metals
US11498123B2 (en) 2015-01-08 2022-11-15 Seiko Epson Corporation Metal powder for powder metallurgy, compound, granulated powder, sintered body, and ornament
CN115487604A (en) * 2022-09-23 2022-12-20 东莞市名创传动科技有限公司 Composite sintered filtering material

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US4602953A (en) * 1985-03-13 1986-07-29 Fine Particle Technology Corp. Particulate material feedstock, use of said feedstock and product
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US3988524A (en) * 1973-01-15 1976-10-26 Cabot Corporation Powder metallurgy compacts and products of high performance alloys
US4129444A (en) * 1973-01-15 1978-12-12 Cabot Corporation Power metallurgy compacts and products of high performance alloys
US4062678A (en) * 1974-01-17 1977-12-13 Cabot Corporation Powder metallurgy compacts and products of high performance alloys
US4121927A (en) * 1974-03-25 1978-10-24 Amsted Industries Incorporated Method of producing high carbon hard alloys
US4070184A (en) * 1976-09-24 1978-01-24 Gte Sylvania Incorporated Process for producing refractory carbide grade powder
US4225345A (en) * 1978-08-08 1980-09-30 Adee James M Process for forming metal parts with less than 1 percent carbon content
US4249944A (en) * 1979-04-09 1981-02-10 Fansteel Inc. Method of making electrical contact material
US4343650A (en) * 1980-04-25 1982-08-10 Cabot Corporation Metal binder in compaction of metal powders
US4663241A (en) * 1980-09-08 1987-05-05 United Technologies Corporation Powder metal disk with selective fatigue strengthening
US4722826A (en) * 1986-09-15 1988-02-02 Inco Alloys International, Inc. Production of water atomized powder metallurgy products
US4834800A (en) * 1986-10-15 1989-05-30 Hoeganaes Corporation Iron-based powder mixtures
DE4101292A1 (en) * 1990-01-17 1991-07-18 Quebec Metal Powders Ltd DETACH-FREE METALLURGICAL POWDER MIXTURES USING A POLYVINYLPYRROLIDONE BINDING AGENT
US5069714A (en) * 1990-01-17 1991-12-03 Quebec Metal Powders Limited Segregation-free metallurgical powder blends using polyvinyl pyrrolidone binder
US5298055A (en) * 1992-03-09 1994-03-29 Hoeganaes Corporation Iron-based powder mixtures containing binder-lubricant
EP0698435A1 (en) 1994-08-24 1996-02-28 Quebec Metal Powders Ltd. Powder metallurgy apparatus and process using electrostatic die wall lubrication
US5498276A (en) * 1994-09-14 1996-03-12 Hoeganaes Corporation Iron-based powder compositions containing green strengh enhancing lubricants
WO1996008329A1 (en) * 1994-09-14 1996-03-21 Hoeganaes Corporation Improved iron-based powder compositions containing green strength enhancing lubricants
US5624631A (en) * 1994-09-14 1997-04-29 Hoeganaes Corporation Iron-based powder compositions containing green strength enhancing lubricants
US6039784A (en) * 1997-03-12 2000-03-21 Hoeganaes Corporation Iron-based powder compositions containing green strength enhancing lubricants
US20040234407A1 (en) * 2003-03-27 2004-11-25 Hoganas Ab Powder metal composition and method for producing components thereof
WO2004085099A1 (en) * 2003-03-27 2004-10-07 Höganäs Ab Cobalt-based metal powder and method for producing components thereof
US20060198751A1 (en) * 2003-03-27 2006-09-07 Hoganas Ab, Co-based water-atomised powder composition for die compaction
US7300488B2 (en) * 2003-03-27 2007-11-27 Höganäs Ab Powder metal composition and method for producing components thereof
US20050044988A1 (en) * 2003-09-03 2005-03-03 Apex Advanced Technologies, Llc Composition for powder metallurgy
WO2005023463A1 (en) * 2003-09-03 2005-03-17 Apex Advanced Technologies, Llc Composition for powder metallurgy
US7192464B2 (en) * 2003-09-03 2007-03-20 Apex Advanced Technologies, Llc Composition for powder metallurgy
US9624568B2 (en) 2008-04-08 2017-04-18 Federal-Mogul Corporation Thermal spray applications using iron based alloy powder
US9162285B2 (en) 2008-04-08 2015-10-20 Federal-Mogul Corporation Powder metal compositions for wear and temperature resistance applications and method of producing same
US9546412B2 (en) * 2008-04-08 2017-01-17 Federal-Mogul Corporation Powdered metal alloy composition for wear and temperature resistance applications and method of producing same
US20090252636A1 (en) * 2008-04-08 2009-10-08 Christopherson Jr Denis B Powdered metal alloy composition for wear and temperature resistance applications and method of producing same
EP2436793A1 (en) * 2008-10-20 2012-04-04 H.C. Starck GmbH Metal powder
US20130306019A1 (en) * 2010-11-09 2013-11-21 Katsunori Otobe High-toughness cobalt-based alloy and engine valve coated with same
US9206715B2 (en) * 2010-11-09 2015-12-08 Fukuda Metal Foil & Powder Co., Ltd. High-toughness cobalt-based alloy and engine valve coated with same
US9796633B2 (en) 2013-10-03 2017-10-24 Kennametal Inc. Aqueous slurry for making a powder of hard material
EP2857124A1 (en) 2013-10-03 2015-04-08 Kennametal Inc. Aqueous slurry for making a powder of hard material
US9475945B2 (en) 2013-10-03 2016-10-25 Kennametal Inc. Aqueous slurry for making a powder of hard material
EP2860274A2 (en) 2013-10-04 2015-04-15 Kennametal India Limited Hard material and method of making the same from an aqueous hard material milling slurry
US10538829B2 (en) 2013-10-04 2020-01-21 Kennametal India Limited Hard material and method of making the same from an aqueous hard material milling slurry
US11498123B2 (en) 2015-01-08 2022-11-15 Seiko Epson Corporation Metal powder for powder metallurgy, compound, granulated powder, sintered body, and ornament
US20170291220A1 (en) * 2016-04-06 2017-10-12 Seiko Epson Corporation Metal powder for powder metallurgy, compound, granulated powder, sintered body, and heat resistant component
WO2021067036A1 (en) * 2019-09-30 2021-04-08 The Penn State Research Foundation Cold sintering process for densification and sintering of powdered metals
CN115487604A (en) * 2022-09-23 2022-12-20 东莞市名创传动科技有限公司 Composite sintered filtering material

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LU69150A1 (en) 1974-04-08
DE2365046A1 (en) 1974-07-18
CS216185B2 (en) 1982-10-29
AR199602A1 (en) 1974-09-13
SE401110B (en) 1978-04-24
BR7400159D0 (en) 1974-08-22
AU6446274A (en) 1975-07-17
JPS5729501A (en) 1982-02-17
DD112725A5 (en) 1975-05-05
GB1457661A (en) 1976-12-08
FR2213826A1 (en) 1974-08-09
FR2213826B1 (en) 1981-02-27
CH587091A5 (en) 1977-04-29
JPS5756523B2 (en) 1982-11-30
IN140276B (en) 1976-10-09
DE2365046C2 (en) 1984-06-07
BE809726A (en) 1974-05-02
NL7400498A (en) 1974-07-17
IT1009104B (en) 1976-12-10
JPS5046507A (en) 1975-04-25
JPS5933654B2 (en) 1984-08-17
HU168185B (en) 1976-03-28
PL88512B1 (en) 1976-09-30
ES422274A1 (en) 1976-07-01
ZA739585B (en) 1974-11-27
ATA27474A (en) 1978-01-15
CA1031603A (en) 1978-05-23

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