US3859086A - Method of enhancing powder compactibility - Google Patents

Method of enhancing powder compactibility Download PDF

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Publication number
US3859086A
US3859086A US214444A US21444471A US3859086A US 3859086 A US3859086 A US 3859086A US 214444 A US214444 A US 214444A US 21444471 A US21444471 A US 21444471A US 3859086 A US3859086 A US 3859086A
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United States
Prior art keywords
powder
particles
powders
process defined
spherical
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Expired - Lifetime
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US214444A
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English (en)
Inventor
Nathan Lewis Church
Edwin Snape
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Huntington Alloys Corp
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International Nickel Co Inc
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Filing date
Publication date
Priority to BE793539D priority Critical patent/BE793539A/fr
Application filed by International Nickel Co Inc filed Critical International Nickel Co Inc
Priority to US214444A priority patent/US3859086A/en
Priority to NL7217440A priority patent/NL7217440A/xx
Priority to CA159,662A priority patent/CA974799A/en
Priority to LU66763A priority patent/LU66763A1/xx
Priority to DE2263858A priority patent/DE2263858A1/de
Priority to FR7246785A priority patent/FR2166166A1/fr
Priority to JP48004512A priority patent/JPS4879108A/ja
Priority to IT55141/72A priority patent/IT974406B/it
Application granted granted Critical
Publication of US3859086A publication Critical patent/US3859086A/en
Anticipated expiration legal-status Critical
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C19/00Alloys based on nickel or cobalt
    • C22C19/03Alloys based on nickel or cobalt based on nickel
    • C22C19/05Alloys based on nickel or cobalt based on nickel with chromium
    • C22C19/051Alloys based on nickel or cobalt based on nickel with chromium and Mo or W
    • C22C19/055Alloys based on nickel or cobalt based on nickel with chromium and Mo or W with the maximum Cr content being at least 20% but less than 30%
    • 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
    • B22F1/145Chemical treatment, e.g. passivation or decarburisation
    • 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
    • B22F2999/00Aspects linked to processes or compositions used in powder metallurgy

Definitions

  • Spherical pre-alloyed powders produced by gas atomization exhibit poor compactibility.
  • Such powders have high strength resulting from the alloy composition and the rapid quench inherent in atomization, such that relatively little deformation of the powder can be attained in conventional powder metallurgy cold pressing operations, even when compacting pressures as high as about 40 or even 70 tons per square inch are resorted to.
  • the pressing problem is so severe that it is even difficult to form such powders into a compressed mass having sufficient green strength to enable removal of the pressed object from the die as a unitary piece.
  • Pre-alloyed, spherical powders exhibiting improved compactibility can be produced by water atomization at relatively low water pressure.
  • wateratomized powders contain high levels of deleterious impurities such as oxygen and oxides.
  • a high-pressure water atomization can be used to produce irregularly shaped, pre-alloyed powders which exhibit relatively good compactibility and have relatively low oxide contents.
  • powder metallurgy products made from such powders exhibit excessive porosity due to the irregular shape of the powders. It is necessaryy to employ long sintering times at high temperatures, e.g., 2 to 4 hours at 2,300F., to close these pores, such longer times and higher temperatures being commercially undesirable and not always effective.
  • an object of the present invention to provide a method of improving the compactibility of pre-alloyed metal powders having a generally spherical shape.
  • Another object of the invention is to provide a method of improving the compactibility and sinterability of pre-alloyed spherical powders without introducing therein deleterious oxygen or oxides.
  • a further object is to provide substantially spherical powders that can be converted to relatively highdensity products with relatively low compacting pressures and sintering temperatures.
  • the present invention comprises subjecting spherical powder particles, particularly those of stainless steel compositions, to selective chemical attack such that substantially only the less chemically resistant surface regions are removed, i.e., selectively removed, so as to roughen the powder surfaces.
  • the chemical attack can be achieved by subjecting the powder surfaces to the action of a corrodent, which can be an acid or an alkali and which is usually in the liquid state, the particular corrodent depending on the material being treated.
  • a corrodent which can be an acid or an alkali and which is usually in the liquid state, the particular corrodent depending on the material being treated.
  • the selective chemical attack provides projections or asperities at the powder surfaces.
  • the depth of removal depends on the corrodent and the time for which chemical attack is carried out, it generally being required that the depth of selective chemical attack be sufficient to weaken the surface layers of the particles so that they can be readily deformed.
  • the depth of selective attack can be about 1 to about 20 microns, height of the resulting surface asperities or projections generally being on the order of such depth of attack.
  • the powders may be rinsed and dried and thereafter compacted at a pressure of, e.g., about 10 to tons per square inch to provide compacts having green densities of, e.g., about 65% to about of theoretical.
  • the green compact can then be sintered, e.g., at about 1,800F. to about 2,100F. or even higher, to provide relatively high density products, this without the need for additives for improving sinterability.
  • the spherical powder particles can be selectively attacked chemically in the as-atomized condition or preparatory steps can be taken to render the particles more susceptible to subsequent selective chemical attack, e.g., by providing two or more metallurgical phases at the surface portions of the particles.
  • Stainless steel powder treatable in accordance with the invention generally contains, by weight, about 12 to 35% chromium, up to about 30% nickel, up to about 0.5% carbon, up to about 0.5% oxygen, up to about 0.2% nitrogen, up to about 0.4% sulphur, up to about 3% copper, up to about 0.4% phosphorus, up to about 2% silicon, up to about 10% manganese, up to about 15% cobalt, up to about 10% molybdenum, up to about 5% tungsten and the balance iron and incidental impurities.
  • stainless steel powder of appropriate composition can be heat treated to render such powders more susceptible to selective chemical attack.
  • Such heat treatment can be employed to produce in the powders one or more active metallurgical phases which can be metallic, e.g., martensite, ferrite and/or austenite.
  • active metallurgical phases can be metallic, e.g., martensite, ferrite and/or austenite.
  • the less chemically resistant phase can comprise, e.g., about 10 to 30 volume or more of the powder.
  • such heat treatment can be carried out by annealing the powder at a temperature of, for example, about l,600 to 2,200F. and, more specifically, about l,800F., to 'obtain an austenite phase dispersed in a ferritic matrix.
  • the annealing preferably is carried out such that the dispersed austenitic phase is of relatively small size and is substantially uniformly distributed throughout the particle surface portions.
  • the selective chemical attack on the thus-treated powders can then be achieved by immersing the powder particles in a corrodent, e.g., boiling aqueous sulfuric acid solution, so as to dissolve the surface regions comprising the less chemically resistant phase thereof. These surface regions preferably are removed to a depth of about to about microns where the average powder size is about 50 to about 150 microns. Thereafter, the powder can be washed, e.g., in water or alcohol, and dried, and subsequently compacted with relative ease, e.g., at 30 t.s.i. pressure, and sintered at, for example, about 2,000 to 2,l00 F. in a hydrogen atmosphere.
  • a corrodent e.g., boiling aqueous sulfuric acid solution
  • spherical stainless steel powder having the composition, by weight, about to 35% chromium, about 0 to 24% nickel, up to about 0.2% carbon, up to about 2% manganese, up to about 2% silicon, up to about 2% carbon, up to about 3% molybdenum, up to about 5% tungsten, and the balance iron and incidental impurities can be provided with a sigma phase dispersed in a matrix of austenite or ferrite by heat treating the powder at about l,200 to 1,700F.
  • the powders can be selectively chemically attacked by immersing the powder particles in a suitable corrodent, e.g., aqueous 70% nitric acid at 70C., so as to dissolve the less chemically resistant sigma phase regions located at the surface portions of the powder particles. Then the thus-treated powders can be rinsed, e.g., in water, dried, compacted at, e.g., 10 to 70 t.s.i., and sintered at about 2,000F., for example.
  • a suitable corrodent e.g., aqueous 70% nitric acid at 70C.
  • spherical powder of austenitic stainless steel composition having the composition, by weight, of about 12 to chromium, about 12 to nickel, up to about 1% silicon, up to about 1.5% molybdenum, up to about 0.2% carbon, up to about 2% tungsten, up to about 2% manganese, up to about 2% cobalt, and the balance iron and incidental impurities and having, for example, an austenitic structure, can be selectively chemically attacked by treating the powder, e.g., for about 10 to 60 minutes, in a bromine-alcohol solution preferably containing about 10 to 20 volume percent bromine.
  • such spherical powders be so pre-treated with acid where the powders include more than 500 p.p.m. oxygen, or even 400, 250, or 100 p.p.m. oxygen where the powder mesh size is l00, +200.
  • the water HCI HNO solution preferably is at a temperature of about 40 to 60C., the etching time depending on the amount of oxide present, e.g., about 1 to 60 minutes.
  • the powder can be rinsed, e.g., in water or alcohol, and dried, and then trated with the bromine-alcohol solution, after which the powders can be compacted at, e.g., 20 or 40 t.s.i. and then sintered at about 2,000 to 2,100F., for example.
  • the oxygen level of a powder will increase with increasing surface area of the powder and, therefore, with decreasing particle diameter.
  • a powder having an average particle radius of about 30 microns has a surface area about twice that of a comparable volume of powder with an average particle radius of about 55 microns.
  • corrodents that can be used to selectively chemically attack stainless steel powders are the following: 1 volume nitric acid in solution in 3 volumes hydrochloric acid; a 10% solution of chromic and hydrochloric acids in water, the amount of chromic acid being increased for more severe attack; ferric chloride, saturated in hydrochloric acid, including a small percentage of nitric acid; 4 parts by weight cupric sulphate and 20 parts by weight hydrochloric acid in solution in 20 parts by weight of water; and a solution of 50% hydrochloric acid in alcohol.
  • selective attack can be carried out with acid solutions containing, e.g., ferric chloride or copper chloride, so as to achieve localized pitting of the powder.
  • powder containing ferrite and another phase e.g., austenite or martensite
  • another phase e.g., austenite or martensite
  • the initial size of the powder particles that are used in practicing the invention is determined by the properties that are sought in the sintered compact.
  • a relatively coarse powder e.g., about 500 microns or larger is generally undesirable because a very deep attack, e.g., 50 microns, which is difficult to achieve, would be required to achieve the degree of surface deformation necessary for rapid sintering of the compacted powders.
  • the required very deep attack would result in a powder compact with poor appearance.
  • too fine an initial powder particle will result in the complete dissolution of many particles or make it difficult to achieve selective attack on a scale fine enough relative to the particle size, to permit ready compaction of the powders.
  • an average powder particle size of about 50 to about microns is preferred.
  • a relatively deep selective attack will not provide any large gain in compactibility but will merely be a waste of metal and corrodent.
  • too shallow a selective attack on the particles will not provide any significant improvement in compactibility and will necessitate longer sintering times.
  • the depth of attack preferably is about 5 to about 15 microns for powder particle sizes of 40 to 400 microns diameter.
  • the attack should be on a sufficiently fine scale, that is, the less chemically resistant surface portions should be uniformly distributed and relatively close together but separated by the more resistant surface regions, so that the maximum number of asperities can be produced, thereby promoting a relatively high degree of interlocking among the treated particles during the compaction process.
  • the particles remain substantially unfragmented with only the occasional very small powder particles being completely dissolved, the larger particles remaining substantially whole except for the selectively removed surface regions.
  • the selectively attacked powder particles substantially retain their spherical configuration but contain deformable microscopic asperities at their surfaces.
  • the present infor one-half hour at 1,700F. in a hydrogen atmosphere to produce in the various powder particles a dispersed austenite phase in a matrix of ferrite. Portions of each annealed sieve fraction were then immersed in a boiling vention is applicable to the treatment of spherical nick- 5 percent sulfuric acid solution in water, for times el-base super-alloy powders containing, by weight, varying from 5 to 60 mmutes, after which the powders about 10 to about chromium, up to about cowere washed in alcohol and dried by warm arr.
  • the varbalt, up to about 25% molybdenum, up to about 10% ious acid-treated portions were then pressed in a die tungsten, up to about 6% columbium, up to about 5% having a cavity with cross-sectional dimensions of onealuminum, up to about 5% titanium, up to about 20% to half inch by 1% inches.
  • the pressure that was applied iron, up to about 1% manganese, up to about 1% silit0 the various powders was either 20 or tons per con, up to about 0.25% carbon, and the balance nickel q a Inch Afterthe Powders were pre ey e e and incidental impurities.
  • powders include austenitic matrices, which can be sethat achieved, this being measured y the green lectively attacked chemically, e.g., by a brominel5' y of the p containing solution, such as an alcohol-l0 to 20 volume Sinteri'ng was conducted for one-half hour at bromine solut1o n, or by a strong oxidizing acid, such 2,050F. in a hydrogen atmosphere.
  • the results obas concentrated nitric acid. tained with the various treated powders are compared
  • Selective chemical attack on such nickel-base superin Table I below with a portion (Powder No. l) of the alloy powders can be enhanced by heat treating the 20 same atomized powder that was annealed in the same powders at, e.g., about l,400 to 2,000 F. to produce way but not subjected to chemical attack.
  • the ornthe powder surfaces a passive film that can be broken p c Of these p wders cracking on handling so that smdown locally at the more active areas by using, e.g., a terlng not camed out f Powder P 1 through solution containing halogen ions, such as HCl.
  • V V minute etch of the 200, +325 powder sieve fractions EXAMPLE (numbers 7 and 9) allowed these powders to be comt pacted but the compacts cracked during the pressing A stifunless Steel Powder havmg t Composition of, operation so that no sintering was carried out for these y Weight, 01% carbon, 80% nickel, 275% chfopowders.
  • a lower sintering temperature can be employed. Such lower sintering temperature, as well as the reduced accessiblity of the interior regions of the compacts to oxygen, attributable to the relatively high densities, reduce the amount of oxidation occurring in the chromium-containing alloys.
  • EXAMPLE II A stainless steel powder composed of, by weight, 0.008% carbon, 0.49% manganese, 022% silicon, 14.7% nickel, 16.8% chromium, 1.5% molybdenum, and the balance essentially iron, was produced by argon atomization at 600 psi argon pressure, of a melt of corresponding composition.
  • the atomized powder which was composed of generally spherical particles was screened to provide a powder fraction of l00, +200 mesh. This powder was then pickled for about 2 minutes in a 50C. solution of parts water 10 parts concentrated HCl 10 parts concentrated HNO to remove surface oxide. The powder was then rinsed in water and then in alcohol and dried in air.
  • the powder was then treated with a solution of volume percent bromine-alcohol for 10 minutes. The powder was again rinsed and dried. The etched powder was then pressed at 40 tons per square inch and sintered for 1 hour at 2,050F. in cracked ammonia. The resulting composition had only 13 percent porosity.
  • Irregularly shaped powder particles of similar composition that were produced by water atomization were compacted and sintered under similar conditions.
  • the sintered compacts produced from this powder exhibited higher porosity, specifically, about 16.5 percent.
  • electrochemical attack can be employed instead of chemical attack, to roughen the powder surfaces.
  • the present invention can be employed to produce various stainless steel powder metallurgy products, including faucet components, marine hardware, including tie-down lugs and capstan components, winches, nuts and brackets.
  • a process for improving the compactibility of metal powders of substantially spherical configuration and of relatively poor initial compactibility comprismg:
  • the metal powder consists of stainless steel consisting essentially of about 12 to about 35% chromium, up to about 30% nickel, up to about 3% copper, up to about 0.5% carbon, up to about 0.5% oxygen, up to about 0.2% nitrogen, up to about 0.4% sulfur, up to about 0.4% phosphorus, up to about 2% silicon, up to about 10% manganese, up to about 15% cobalt, up to about 10% molybdenum, up to about 5% tungsten, and the balance iron.
  • the preliminary heat treatment comprises annealing the powders so as to produce therein a metallurgical structure of austenite dispersed in a ferrite matrix.
  • the powder consists essentially of, by weight, about 20 to about 35% chromium, about 0 to about 24% nickel, up to about 0.2% carbon, up to about 2% manganese, up to about 2% silicon, up to about 2% cobalt, up to about 3% molybdenum, up to about 5% tungsten, and the balance essentially iron and the preliminary heat treatment is carried out to produce in the powder two metallurgical phases respectively comprising sigma phase and one of austenite and ferrite, the sigma phase being dispersed in a matrix of one of said ferrite and austenite phases.
  • iron up to about 1% manganese, up to about 1% silicon, up to about 0.25% carbon, and the balance nickel.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Powder Metallurgy (AREA)
  • Manufacture Of Metal Powder And Suspensions Thereof (AREA)
US214444A 1971-12-30 1971-12-30 Method of enhancing powder compactibility Expired - Lifetime US3859086A (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
BE793539D BE793539A (fr) 1971-12-30 Perfectionnements relatifs a la compression des poudres
US214444A US3859086A (en) 1971-12-30 1971-12-30 Method of enhancing powder compactibility
CA159,662A CA974799A (en) 1971-12-30 1972-12-21 Method of enhancing powder compactibility
NL7217440A NL7217440A (fr) 1971-12-30 1972-12-21
LU66763A LU66763A1 (fr) 1971-12-30 1972-12-28
DE2263858A DE2263858A1 (de) 1971-12-30 1972-12-28 Verfahren zur verbesserung der verdichtbarkeit und des sinterverhaltens fertiglegierter sphaerolithischer metallpulver
FR7246785A FR2166166A1 (fr) 1971-12-30 1972-12-28
JP48004512A JPS4879108A (fr) 1971-12-30 1972-12-29
IT55141/72A IT974406B (it) 1971-12-30 1972-12-29 Procedimento per agglomerare polve ri e prodotti da esso ottenuti

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US214444A US3859086A (en) 1971-12-30 1971-12-30 Method of enhancing powder compactibility

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US (1) US3859086A (fr)
JP (1) JPS4879108A (fr)
BE (1) BE793539A (fr)
CA (1) CA974799A (fr)
DE (1) DE2263858A1 (fr)
FR (1) FR2166166A1 (fr)
IT (1) IT974406B (fr)
LU (1) LU66763A1 (fr)
NL (1) NL7217440A (fr)

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4310611A (en) * 1979-06-29 1982-01-12 Eastman Kodak Company Electrographic magnetic carrier particles
US4483819A (en) * 1981-07-31 1984-11-20 Hermann C. Starck Berlin Production of highly capacitive agglomerated valve metal powder and valve metal electrodes for the production of electrolytic capacitors
US4581202A (en) * 1984-03-12 1986-04-08 Sumitomo Metal Industries, Ltd. Sintered stainless steel and production process therefor
US4587096A (en) * 1985-05-23 1986-05-06 Inco Alloys International, Inc. Canless method for hot working gas atomized powders
GB2207442A (en) * 1987-07-09 1989-02-01 Inco Alloys Int Method for surface activation of water atomized powders by pickling prior to compacting
US4960459A (en) * 1987-07-09 1990-10-02 Inco Alloys International, Inc. Method for surface activation of water atomized powders by pickling
US5427600A (en) * 1992-11-30 1995-06-27 Sumitomo Electric Industries, Ltd. Low alloy sintered steel and method of preparing the same
US5869196A (en) * 1996-12-20 1999-02-09 Composite Material Technology, Inc. Constrained filament electrolytic anode and process of fabrication
US6042781A (en) * 1991-12-04 2000-03-28 Materials Innovation, Inc. Ambient temperature method for increasing the green strength of parts
US6537489B2 (en) * 2000-11-09 2003-03-25 Höganäs Ab High density products and method for the preparation thereof
US20040112173A1 (en) * 2001-01-24 2004-06-17 Paritosh Maulik Sintered ferrous material contaning copper
US20050129563A1 (en) * 2003-12-11 2005-06-16 Borgwarner Inc. Stainless steel powder for high temperature applications
US20070072039A1 (en) * 2005-09-26 2007-03-29 Samsung Sdi Co., Ltd. Metallic separator for fuel cell
US20110162612A1 (en) * 2010-01-05 2011-07-07 L.E. Jones Company Iron-chromium alloy with improved compressive yield strength and method of making and use thereof
US20190309399A1 (en) * 2016-12-07 2019-10-10 Höganäs Ab (Publ) Stainless steel powder for producing duplex sintered stainless steel
US11059102B2 (en) 2016-03-15 2021-07-13 KSB SE & Co. KGaA Method for producing components from a duplex steel, and components produced using said method
US20240033822A1 (en) * 2020-08-19 2024-02-01 Yuanyun ZHAO Method for preparing high-purity powder material, application thereof, and double-phase powder material
US12351894B2 (en) 2020-03-26 2025-07-08 Vdm Metals International Gmbh Powder made of a cobalt-chromium alloy

Families Citing this family (3)

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US3933961A (en) * 1974-12-13 1976-01-20 Pennwalt Corporation Tabletting spherical dental amalgam alloy
DE3831091A1 (de) * 1988-09-13 1990-03-29 Basf Ag Oxidbeschichtete carrier, ein verfahren zur herstellung dieser carrier und deren verwendung
US5112572A (en) * 1991-10-01 1992-05-12 Inco Limited Deoxidation treatment for consolidated atomized metal powder

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US1913133A (en) * 1931-06-10 1933-06-06 Copper Deoxidation Corp Coalescence of metals
US2527611A (en) * 1943-03-17 1950-10-31 Wulff John Method of producing metal powders
US3407063A (en) * 1963-10-07 1968-10-22 Atomic Energy Authority Uk Hot-pressing of metal powders having inert solid surface films by adding activator elements

Patent Citations (3)

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Publication number Priority date Publication date Assignee Title
US1913133A (en) * 1931-06-10 1933-06-06 Copper Deoxidation Corp Coalescence of metals
US2527611A (en) * 1943-03-17 1950-10-31 Wulff John Method of producing metal powders
US3407063A (en) * 1963-10-07 1968-10-22 Atomic Energy Authority Uk Hot-pressing of metal powders having inert solid surface films by adding activator elements

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4310611A (en) * 1979-06-29 1982-01-12 Eastman Kodak Company Electrographic magnetic carrier particles
US4483819A (en) * 1981-07-31 1984-11-20 Hermann C. Starck Berlin Production of highly capacitive agglomerated valve metal powder and valve metal electrodes for the production of electrolytic capacitors
US4581202A (en) * 1984-03-12 1986-04-08 Sumitomo Metal Industries, Ltd. Sintered stainless steel and production process therefor
US4587096A (en) * 1985-05-23 1986-05-06 Inco Alloys International, Inc. Canless method for hot working gas atomized powders
GB2207442A (en) * 1987-07-09 1989-02-01 Inco Alloys Int Method for surface activation of water atomized powders by pickling prior to compacting
US4818482A (en) * 1987-07-09 1989-04-04 Inco Alloys International, Inc. Method for surface activation of water atomized powders
US4960459A (en) * 1987-07-09 1990-10-02 Inco Alloys International, Inc. Method for surface activation of water atomized powders by pickling
GB2207442B (en) * 1987-07-09 1991-06-19 Inco Alloys Int Method for surface activation of water atomized powders
US6042781A (en) * 1991-12-04 2000-03-28 Materials Innovation, Inc. Ambient temperature method for increasing the green strength of parts
US5427600A (en) * 1992-11-30 1995-06-27 Sumitomo Electric Industries, Ltd. Low alloy sintered steel and method of preparing the same
US5869196A (en) * 1996-12-20 1999-02-09 Composite Material Technology, Inc. Constrained filament electrolytic anode and process of fabrication
US6537489B2 (en) * 2000-11-09 2003-03-25 Höganäs Ab High density products and method for the preparation thereof
US20040112173A1 (en) * 2001-01-24 2004-06-17 Paritosh Maulik Sintered ferrous material contaning copper
US20050129563A1 (en) * 2003-12-11 2005-06-16 Borgwarner Inc. Stainless steel powder for high temperature applications
US8148034B2 (en) * 2005-09-26 2012-04-03 Samsung Sdi Co., Ltd. Metallic separator for fuel cell
US20070072039A1 (en) * 2005-09-26 2007-03-29 Samsung Sdi Co., Ltd. Metallic separator for fuel cell
US20110162612A1 (en) * 2010-01-05 2011-07-07 L.E. Jones Company Iron-chromium alloy with improved compressive yield strength and method of making and use thereof
US8479700B2 (en) 2010-01-05 2013-07-09 L. E. Jones Company Iron-chromium alloy with improved compressive yield strength and method of making and use thereof
US11059102B2 (en) 2016-03-15 2021-07-13 KSB SE & Co. KGaA Method for producing components from a duplex steel, and components produced using said method
US20190309399A1 (en) * 2016-12-07 2019-10-10 Höganäs Ab (Publ) Stainless steel powder for producing duplex sintered stainless steel
US12351894B2 (en) 2020-03-26 2025-07-08 Vdm Metals International Gmbh Powder made of a cobalt-chromium alloy
US20240033822A1 (en) * 2020-08-19 2024-02-01 Yuanyun ZHAO Method for preparing high-purity powder material, application thereof, and double-phase powder material
US12409494B2 (en) * 2020-08-19 2025-09-09 Yuanyun ZHAO Method for preparing high-purity powder material, application thereof, and double-phase powder material

Also Published As

Publication number Publication date
FR2166166A1 (fr) 1973-08-10
IT974406B (it) 1974-06-20
CA974799A (en) 1975-09-23
JPS4879108A (fr) 1973-10-24
DE2263858A1 (de) 1973-07-12
LU66763A1 (fr) 1973-07-18
BE793539A (fr) 1973-06-29
NL7217440A (fr) 1973-07-03

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