US3476548A - Method for removing oxides from alloy powder - Google Patents
Method for removing oxides from alloy powder Download PDFInfo
- Publication number
- US3476548A US3476548A US600379A US3476548DA US3476548A US 3476548 A US3476548 A US 3476548A US 600379 A US600379 A US 600379A US 3476548D A US3476548D A US 3476548DA US 3476548 A US3476548 A US 3476548A
- Authority
- US
- United States
- Prior art keywords
- powder
- water
- alloy
- compacting
- drying agent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/14—Treatment of metallic powder
- B22F1/145—Chemical treatment, e.g. passivation or decarburisation
Definitions
- the alloy particles are subjected to a treatment in molten caustic, acid pickling and mechanical scale breaking, such as sonic vibration. These operations may be performed singly or in combination depending upon how difiicult the oxide of the particular alloy is to remove. The more difiicult or complex the alloy, the more severe must be the treatment.
- a charge of alloy particles which are intended for subsequent use in compacting into alloy articles, are placed in a bath of molten caustic.
- Any of the well-known caustics such as sodium hydroxide and potassium hydroxide, may be used.
- the molten caustic is typically at a temperature of about 1000? F., and the powder is maintained therein for about 15 minutes.
- the particles are removed from the caustic and rinsed with water to remove excess caustic therefrom. Thereafter, the particles are transferred to an acid pickling bath, which may be, for example, hydrochloric acid or sulfuric acid.
- acid pickling the powder is preferably subjected to sonic vibration to insure complete contact of the particle surface area with the acid. After pickling the particles are rinsed with water to remove excess acid. It is to be understood, of course, that more than one pickling operation, followed by water rinsing, may be employed.
- the particles After the particles have been pickledl and the excess acid removed by water rinsing, they are, of course, saturated with water. Upon exposure to the atmosphere in this condition, the surfaces of the powder, which have been cleaned of surface oxides by the treatment described above, will begin to reoxidize. Because these oxides, as explained above, are difficult to remove, adequate removal of oxides, particularly oxides of titanium and aluminum, thus formed will not result by merely placing the powder in an evacuated container and heating the same to an elevated temperature prior to compacting, which is a customary practice in powder metallurgy. Consequently, it is essential, if an oxygen-free article is to be produced, to protect the cleaned powders from reoxidation while exposed to oxidizing atmospheres prior to compacting.
- the cleaned particles after being subjected to the above-described oxide removal operation, are dried (water removed) and protected from further oxidation in the following manner.
- the wet particles are placed in a container, preferably that which is to be used during subsequent heating, evacuation, and compacting.
- the water is then displaced by the addition of an agent, such as methylene chloride.
- Methylene chyloride, or any drying agent substituted therefor, such as hexane or toluol must have the properties of zero solubility for water, high vapor pressure, and be heavier than water.
- the methylene chloride provides a barrier between the surface of the powder and the surrounding air.
- the powder may then be placed in a chamber for evacuation and heating to elevated temperature whereupon, in the conventional manner, pressure may be applied to compact the powder into the desired alloy article. Since methylene chloride has zero solubility for water, no oxygen which would otherwise be present from any water dissolved in the methylene chloride is present during the heating operation.
- the high vapor pressure of the agent as indicated by its low boiling point of 40 C., insures complete removal of the agent from the powder during evacation and prior to compacting.
- the vapor pressure of the drying agent must be sufficiently high so that at the temperatures and pressures prevailing in a particular operation, the drying agent will be completely removed prior to compacting.
- drying agent If the drying agent is not completely removed prior to compacting, such will result in contamination of the final compacted article. It may be seen, therefore, that in accordance with the method of the invention as outlined above dry, clean, oxide-free powders are protected against reoxidation prior to compacting to result in a compacted article having an extremely low oxygen content and a corresponding high degree of cleanliness.
- a charge of a mesh powder of a precipitation hardenable, nickel-chromium base alloy having in percent by weight- 12.50 chromium, 4.20 molybdenum, 2.20 columbium and tantalum, 6.10 aluminum, 0.80 titanium, 0.12 carbon, 0.012 boron, 0.10 zirconium, and balance nickel in a 100 gram quantity was poured into a sealed end of a A in. pipe about 3 ft. in length. Steel wool was then tapped on top of the charge to secure it at the bottom 2 inches of the pipe. The open end of the pipe was connected to a vacuum pump and pumping was begun and continued until the outgassing rate stabilized (about 1 micron per minute). About 12 to 14 in.
- the polished specimens were examined at magnifications of about 400 Prior to the above-described treatment, the powder was cleaned by treatment in a hot sodium hydroxide bath (about 850900 F.) for approximately 15 minutes, water rinsed to remove excess caustic, placed in bath of hydrochloric acid (160180 F.) for approximately 5 minutes while being subjected to sonic vibration, and water rinsed.
- a hot sodium hydroxide bath about 850900 F.
- water rinsed to remove excess caustic placed in bath of hydrochloric acid (160180 F.) for approximately 5 minutes while being subjected to sonic vibration, and water rinsed.
- the powder was divided into a number of 100-gram charges, which were air dried and subjected to the above treatment. Polished specimens of this material exhibited 85-90 percent oxide-free particle boundaries.
- a method for producing a charge of alloy powder free of complex surface oxides for use in compacting to form an alloy article comprising treating said powder with molten caustic, water rinsing said powder to remove excess caustic, acid pickling said powder, water rinsing said powder to remove excess acid, removing the water from said powder by displacing the same with a dry ng agent, said drying agent being heavier than water, havmg substantially zero solubility for water and high vapor pressure, whereby said drying agent provides a barrier between the chemically clean surfaces of the powder and the oxidizing atmosphere.
- drying agent is methylene chloride
- said alloy powder contains an amount of at least one alloying ele- 0 ment selected from a group consisting of titanium and aluminum.
- drying agent is selected from a group consisting of methylene chloride, hexane, and toluol.
- a method for producing a charge of alloy powder free of complex surface oxides for use in compacting to form an alloy article comprising treating said powder with molten caustic, rinsing said powder to remove excess caustic, acid pickling said powder, water rinsing said powder to remove excess acid, removing the water from said powder by displacing the same with a drying agent, said drying agent being heavier than water, having substantially zero solubility for water and high vapor pressure whereby said drying agent provides a barrier between the chemically clean surfaces of the powder and the oxidizing atmosphere, charging said powder saturated with said drying agent to a gas-tight container to remove said drying agent by vaporization thereof, whereby said charge of alloy powder is dry and free of complex oxides and prepared for compacting.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US60037966A | 1966-12-09 | 1966-12-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3476548A true US3476548A (en) | 1969-11-04 |
Family
ID=24403354
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US600379A Expired - Lifetime US3476548A (en) | 1966-12-09 | 1966-12-09 | Method for removing oxides from alloy powder |
Country Status (1)
Country | Link |
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US (1) | US3476548A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2137862A1 (en) * | 1971-05-14 | 1972-12-29 | Hoeganaes Ab | |
EP0535824A1 (en) * | 1991-10-01 | 1993-04-07 | Inco Limited | Deoxidation treatment for atomized metal powder |
US11440094B2 (en) * | 2018-03-13 | 2022-09-13 | Mueller Industries, Inc. | Powder metallurgy process for making lead free brass alloys |
US11459639B2 (en) * | 2018-03-13 | 2022-10-04 | Mueller Industries, Inc. | Powder metallurgy process for making lead free brass alloys |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2027532A (en) * | 1934-04-04 | 1936-01-14 | Hardy Metallurg Company | Powder metallurgy |
US2458661A (en) * | 1944-01-29 | 1949-01-11 | J H Shoemaker | Process of cleaning metal surfaces and compositions therefor |
US2567456A (en) * | 1947-04-07 | 1951-09-11 | J H Shoemaker | Metal cleaning composition and process |
US2630393A (en) * | 1948-06-25 | 1953-03-03 | Charles B Francis | Method of cleaning and descaling ferrous bodies |
US2638424A (en) * | 1946-02-09 | 1953-05-12 | American Electro Metal Corp | Method of processing metal powders |
-
1966
- 1966-12-09 US US600379A patent/US3476548A/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2027532A (en) * | 1934-04-04 | 1936-01-14 | Hardy Metallurg Company | Powder metallurgy |
US2458661A (en) * | 1944-01-29 | 1949-01-11 | J H Shoemaker | Process of cleaning metal surfaces and compositions therefor |
US2638424A (en) * | 1946-02-09 | 1953-05-12 | American Electro Metal Corp | Method of processing metal powders |
US2567456A (en) * | 1947-04-07 | 1951-09-11 | J H Shoemaker | Metal cleaning composition and process |
US2630393A (en) * | 1948-06-25 | 1953-03-03 | Charles B Francis | Method of cleaning and descaling ferrous bodies |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2137862A1 (en) * | 1971-05-14 | 1972-12-29 | Hoeganaes Ab | |
EP0535824A1 (en) * | 1991-10-01 | 1993-04-07 | Inco Limited | Deoxidation treatment for atomized metal powder |
US11440094B2 (en) * | 2018-03-13 | 2022-09-13 | Mueller Industries, Inc. | Powder metallurgy process for making lead free brass alloys |
US11459639B2 (en) * | 2018-03-13 | 2022-10-04 | Mueller Industries, Inc. | Powder metallurgy process for making lead free brass alloys |
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Owner name: COLT INDUSTRIES OPERATING CORP. Free format text: MERGER AND CHANGE OF NAME;ASSIGNOR:CRUCIBLE CENTER COMPANY (INTO) CRUCIBLE INC. (CHANGED TO);REEL/FRAME:004120/0308 Effective date: 19821214 |
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Owner name: CRUCIBLE MATERIALS CORPORATION, PENNSYLVANIA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:COLT INDUSTRIES OPERATING CORP.;REEL/FRAME:004194/0621 Effective date: 19831025 Owner name: CRUCIBLE MATERIALS CORPORATION, A DE CORP. Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:COLT INDUSTRIES OPERATING CORP.;REEL/FRAME:004194/0621 Effective date: 19831025 |
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Owner name: MELLON BANK, N.A. FOR THE CHASE MANHATTAN BANK (NA Free format text: SECURITY INTEREST;ASSIGNOR:CRUCIBLE MATERIALS CORPORATION, A CORP. OF DE.;REEL/FRAME:004490/0452 Effective date: 19851219 Owner name: CHASE MANHATTAN BANK, THE (NATIONAL ASSOCIATION) A Free format text: SECURITY INTEREST;ASSIGNOR:CRUCIBLE MATERIALS CORPORATION, A CORP. OF DE.;REEL/FRAME:004490/0452 Effective date: 19851219 Owner name: MELLON FINANCIAL SERVICES CORPORATION Free format text: SECURITY INTEREST;ASSIGNOR:CRUCIBLE MATERIALS CORPORATION, A CORP. OF DE.;REEL/FRAME:004490/0410 Effective date: 19851219 Owner name: MELLON BANK, N.A. AS AGENT FOR MELLON BANK N.A. & Free format text: SECURITY INTEREST;ASSIGNOR:CRUCIBLE MATERIALS CORPORATION, A CORP. OF DE.;REEL/FRAME:004490/0410 Effective date: 19851219 |