WO2000021703A1 - Method of producing sintered body - Google Patents
Method of producing sintered body Download PDFInfo
- Publication number
- WO2000021703A1 WO2000021703A1 PCT/JP1999/005599 JP9905599W WO0021703A1 WO 2000021703 A1 WO2000021703 A1 WO 2000021703A1 JP 9905599 W JP9905599 W JP 9905599W WO 0021703 A1 WO0021703 A1 WO 0021703A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- extrusion
- sintered body
- binder
- temperature
- melting point
- 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.)
- Ceased
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Classifications
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- 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
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/22—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip
- B22F3/227—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip by organic binder assisted extrusion
-
- 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
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/20—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces by extruding
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- 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
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/22—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip
-
- 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
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/12—Both compacting and sintering
- B22F3/14—Both compacting and sintering simultaneously
- B22F2003/145—Both compacting and sintering simultaneously by warm compacting, below debindering temperature
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- 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
- B22F2998/00—Supplementary information concerning processes or compositions relating to powder metallurgy
-
- 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
- B22F2998/00—Supplementary information concerning processes or compositions relating to powder metallurgy
- B22F2998/10—Processes characterised by the sequence of their steps
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- 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
- B22F2999/00—Aspects linked to processes or compositions used in powder metallurgy
Definitions
- the present invention relates to a method for producing a sintered body obtained by sintering a compact of metal powder.
- Hot extrusion processing in which a metal material is extruded from an extrusion die and formed into a predetermined shape. Thereby, for example, a long metal product can be manufactured.
- An object of the present invention is to provide a method for manufacturing a sintered body that can easily obtain a metal product (particularly, a long product or a cut product thereof) with a wide degree of freedom of usable metals and high dimensional accuracy. It is in. Disclosure of the invention
- the present invention provides a step of extruding a composition containing a metal powder and a binder by extruding the composition from an extrusion die of an extruder,
- a temperature gradient is provided in the extrusion die along an extrusion direction.
- the composition preferably contains an organic material having a lower melting point than the binder.
- the organic material preferably has a function as a binder.
- the melting point of the binder is preferably 80 to 300 ° C, and the melting point of the organic material is preferably 150 to 80 ° C.
- the extrusion molding is performed by setting the temperature near the extrusion port of the extrusion die lower than the melting point of the binder and higher than the melting point of the organic material.
- the extrusion molding is preferably performed by adjusting the temperature near the extrusion port of the extrusion die by a cooling device and a heating device.
- the step of degreasing preferably includes a first step of degreasing in a low temperature range and a second step of degreasing in a higher temperature range than the first step.
- FIG. 1 is a cross-sectional view showing a configuration example of an extrusion molding machine used in the present invention.
- FIG. 2 is a cross-sectional view showing an extrusion die (die) of the extrusion molding machine shown in FIG. 1 and the vicinity thereof.
- FIG. 3 is a graph showing an example of a change over time in the furnace temperature during the degreasing treatment in the present invention. Explanation of reference numerals
- the composition used in the present invention includes a metal powder and a binder (binder), and preferably further includes an organic material having a lower melting point than the binder.
- metal material constituting the metal powder is not particularly limited.
- metal material Fe, Ni, Co, Cr, Mn, Zn, Pt, Au, Ag , Cu, Pd, Al, W, Ti, V, Mo, Nb, Zr, Pr, Nd, Sm, etc., or at least one of these (including Alloys).
- metal powder stainless steel (for example, SU S304, SUS316, SUS317, SUS329J1, SUS410, SUS430, SUS440, SUS630), die steel
- Fe-based alloys for example, SU S304, SUS316, SUS317, SUS329J1, SUS410, SUS430, SUS440, SUS630
- Ti or Ti-based alloys such as speed tool steels, W or W-based alloys, Co-based cemented carbides, and Ni-based cermets.
- Metals other than Ti constituting the Ti-based alloy include, for example, Fe, Ni, Cr, Pd, Co, Zr, Al, V, Mo, Sn, Au, Ag, and Cu. One or more of them may be mentioned. In this case, the total content of metals other than Ti is preferably not more than 60 wt%, more preferably less than 50 wt%.
- the average particle size of the metal powder is not particularly limited, but is preferably 150 ⁇ m or less, and usually more preferably about 0.1 to 60 ⁇ m. If the average particle size is too large, the sintering density may decrease depending on other conditions.
- the method for producing the metal powder is not particularly limited. For example, those produced by a water or gas atomization method, a reduction method, a carbonyl method, or a pulverization method can be used. You.
- binder examples include polyolefins such as polyethylene, polypropylene, and ethylene-vinyl acetate copolymer, acrylic resins such as polymethyl methacrylate and polybutyl methacrylate, styrene resins such as polystyrene, polyvinyl chloride, and polyvinylidene chloride. And various resins such as polyamide, polyester, polyester, polyester alcohol, and a copolymer thereof, and one or more of these can be used in combination.
- the organic material is not particularly limited as long as it has an melting point lower than that of the binder used.
- the organic material preferably has a function as a binder.
- examples of the organic material having the function of a binder include wax and paraffin.
- the function (such as bonding strength) of the organic material as a binder may be lower than that of the binder.
- the melting point of the binder is preferably about 80 to 300 ° C, more preferably about 80 to 250 ° C. Is more preferable.
- the melting point of the organic material is preferably about 150 to 80 ° C., and more preferably about 40 to 60 ° C.
- the metal powder and the binder are prepared, preferably, the metal powder, the binder, and the organic material are prepared, and these are kneaded by a kneader to obtain a kneaded product (compound).
- a lubricant for example, an antioxidant, a degreasing accelerator, and a surfactant can be added as necessary.
- the kneading conditions vary depending on various conditions such as the metal composition and particle size of the metal powder to be used, the composition of the binder and the organic material, and the compounding amounts thereof.
- the kneading temperature is about 50 to 250 ° C.
- Kneading time about 20 to 210 minutes.
- the kneaded material is pelletized as necessary.
- the particle size of the pellets is, for example, about 1-10.
- extrusion is performed by an extruder. It is molded to produce molded articles of desired shape (cross-sectional shape) and dimensions.
- a temperature gradient is provided stepwise or continuously in an extrusion die (die) of the extruder along the extrusion direction, preferably so that the temperature at the extrusion port side is lowered. I do.
- the shape and dimensions of the manufactured compact are determined in consideration of the amount of shrinkage of the compact due to degreasing and sintering.
- FIG. 1 is a cross-sectional view illustrating a configuration example of an extruder used in the present invention
- FIG. 2 is a cross-sectional view illustrating an extrusion die (die) of the extruder illustrated in FIG. 1 and its vicinity.
- the left side in FIGS. 1 and 2 is referred to as “tip” and the right side is referred to as “base end”.
- the extruder 1 shown in these figures is a screw-type extruder, a base not shown, a cylinder 2 supported on the base, adapter plates 61 and 62, and a breaker ring. 4, an extrusion die (die) 5, a screw 3 rotating in the cylinder 2, a drive mechanism (not shown) for rotating the screw 3, and a hopper for storing the compound and supplying it to the cylinder 12 7 and.
- the breaker ring 4 and the extrusion die 5 are connected to the tip of the cylinder 12 via the adapter plates 61 and 62 while being sandwiched between the adapter plate 61 and the adapter plate 62. In this case, a breaker ring 4 is located between the cylinder 2 and the extrusion die 5.
- the adapter plate 61 and the adapter plate 62 are connected by screws (not shown).
- a heating device (heating device) 21 is installed around the outside of the cylinder 2.
- the extrusion die 5 is composed of an injection-side die 51 having a tapered portion whose inner diameter is reduced toward the extrusion-port side, and an extrusion-side die 52 that regulates the shape of the molded body. It is configured.
- the injection-side die 51 and the extrusion-side die 52 are joined so that these hollow portions communicate with each other.
- a heater (heating device) 53 is provided on the outer periphery of the inlet-side die 51.
- a heater (heating device) 54 is provided on the outer periphery of the extrusion-side die 52, and a cooling device 55 is provided at the tip (end surface on the push-out side).
- the compound (not shown) put into the hopper 7 is supplied into the cylinder 12.
- the screw 3 is driven to rotate at a predetermined rotation speed (rotation speed) in a predetermined direction by a driving mechanism.
- the rotation speed of the screw 3 is not particularly limited, but is preferably, for example, about l to 250 rpm.
- Cylinder 1 and inlet-side die 51 are heated to a predetermined temperature distribution by heaters 21 and 53, respectively, and while the compound is transferred to the front end side in cylinder 2, It is heated to a temperature higher than the melting temperature (melting point) of the binder (thermoplastic resin) in the compound and melts.
- the melt of this compound is reduced in viscosity to improve fluidity, and pores are eliminated by consolidation.
- the temperatures of the cylinder 2 and the inlet-side die 51 are not particularly limited, and are appropriately set depending on the binder, the organic material, and the like to be used, but are preferably about 100 to 400 ° C., and about 120 ° C. A temperature of about 350 ° C. is more preferable.
- the melt of the compound is supplied into the breaker ring 4 from the tip of the cylinder 2, transferred to the extrusion die 5 side through the breaker ring 4, and injected into the extrusion die 5 from the tip of the breaker ring 4. Is done.
- the melt of the compound injected into the extrusion die 5 is continuously extruded from the extrusion die 5 and formed into a predetermined shape.
- the temperature of the extrusion port die 52 is adjusted to a predetermined temperature distribution by the cooling device 55 and the heater 54 so that the melt of the compound can be cooled and solidified.
- the die 52 on the outlet side is cooled by the cooling device 55, and conversely, the temperature of the die 52 on the outlet side is lower than the target temperature.
- the extrusion die 52 is heated with a heater 54.
- the molded body 100 is cut into a desired length, whereby a molded body having a desired shape and dimensions is obtained.
- the temperature of the die 52 on the extrusion port side is preferably lower than the temperature of the die 51 on the injection port side (the temperature near the injection port of the extrusion die 5). It is preferably lower than the melting point of the organic material and higher than the melting point of the organic material.
- the temperature of the extrusion port side die 52 is not particularly limited, and is appropriately set depending on a binder, an organic material, and the like to be used, but is preferably about 30 to 120 ° C, and is preferably about 30 to 90 ° C. Is more preferred.
- the extrusion pressure is preferably at most 100 kg / cm 2 , more preferably at most 500 kg / cm 2 .
- the extrusion speed is preferably about 0.1 to 50 band / sec, more preferably about 0.2 to 20 mm / sec.
- the cross-sectional shape of the compact is determined by selecting the shape of the extrusion port of the extrusion die 5. It is.
- the extrusion die 5 is composed of a single die, a rod-like or plate-like molded product (finally a metal product) such as a cylinder can be obtained. If the extrusion die 5 is composed of an outer die and an inner die, A hollow shaped body such as a cylinder (finally a metal product) is obtained. In addition, by selecting the shape of the extrusion outlet of the extrusion die 5, it is possible to easily manufacture a thin-walled or irregular-shaped one. Further, by adjusting the cutting length of the molded body 100, a molded body (finally, a metal product) of any length from flat to long can be manufactured. In the above, the screw-type extruder has been representatively described. However, the present invention is not limited to this.
- the extruder may be extruded using a ram extruder.
- This ram extruder has a structure in which the screw 3 in the extruder 1 shown in FIG. 1 is replaced with a biston that reciprocates in a cylinder 2.
- the hopper 7 may store a mixture of the above-described compositions, and supply the mixture to the cylinder 12.
- the molded body obtained in the step [2A] is subjected to a degreasing treatment (a debinding treatment).
- a non-oxidizing atmosphere such as a vacuum or under reduced pressure (1 X 1 0- 1 ⁇ 1 X 1 0- 6 Torr For example), or nitrogen gas, in inert gas such as argon gas
- inert gas such as argon gas
- the heat treatment is preferably performed at a temperature of about 150 to 75 ° C for about 0.5 to 40 hours, and more preferably for a temperature of about 250 to 65 ° C for 1 to 24 hours. It is about time.
- Degreasing by such a heat treatment may be performed in various steps (steps) for various purposes (for example, for shortening the degreasing time).
- steps for example, a method of performing a degreasing treatment at a low temperature in the first half and a high temperature in the second half, and a method of repeatedly performing a low temperature and a high temperature are exemplified.
- the compact contains a metal powder, a binder, and an organic material
- the decomposition temperature of a resin or the like has a correlation with its melting point, and the decomposition temperature of the organic material in the molded body is lower than the decomposition temperature of the binder. Therefore, at the time of degreasing, first, an organic material having a low decomposition temperature is decomposed and removed in a first step, and then, a binder having a high decomposition temperature is decomposed and removed in a second step. In this second step, the binder is removed through voids (voids) formed by decomposing and removing the organic material.
- the heat treatment conditions in the first step are preferably at a temperature of about 100 to 400 ° C. for about 0.5 to 30 hours, more preferably at a temperature of about 150 to 350 ° C .: ! It takes about 20 hours.
- the heat treatment in the second step is preferably performed at a temperature of about 250 to 75 ° C. for about 0.5 to 35 hours, more preferably at a temperature of about 150 to 350 ° C. It takes about 1 to 24 hours.
- the degreasing treatment may be performed by eluting a specific component in the binder, the organic material, and the additive using a predetermined solvent (liquid or gas).
- the degreased body (degreased molded body) obtained in the step [3A] is fired and sintered in a sintering furnace to produce a metal sintered body (sintered body).
- the metal powder diffuses and grows to form crystal grains, whereby a dense sintered body having a high density and a low porosity can be obtained.
- the sintering temperature in sintering is not particularly limited.
- the metal composition is Fe or an Fe-based alloy, it is preferably about 950 to 150 ° C., and more preferably about 110 ° C.
- the sintering time is preferably about 0.5 to 8 hours, more preferably about 1 to 5 hours at the sintering temperature as described above.
- the sintering atmosphere is preferably a non-oxidizing atmosphere. This contributes to a reduction in the porosity of the sintered body.
- the preferred sintering atmosphere is lxl O— 2 Torr or less (more preferably 1 ⁇ 1
- one 2 ⁇ LXL O-vacuum (vacuum) under 6 Torr) or 1 ⁇ 76 OTorr nitrogen gas is preferably an inert gas atmosphere or 1-76 OTorr hydrogen gas atmosphere, such as argon gas.
- the sintering atmosphere may change during sintering. For example, initially a reduced pressure (vacuum) under 1 X 10 one 2 ⁇ 1 X 1 0- 6 Torr , can be switched to an inert gas such as the halfway.
- a reduced pressure (vacuum) under 1 X 10 one 2 ⁇ 1 X 1 0- 6 Torr can be switched to an inert gas such as the halfway.
- Sintering under the above conditions contributes to further reduction of porosity, that is, higher density of the sintered body, high dimensional accuracy, and high sintering efficiency. Sintering can be performed in a shorter sintering time, and productivity is also improved.
- the sintering may be performed in two or more stages. For example, first sintering and second sintering with different sintering conditions can be performed. In this case, the sintering temperature of the second sintering can be higher than the sintering temperature of the first sintering. Thereby, the efficiency of sintering is further improved, and the porosity can be further reduced.
- the composition includes a metal powder, a binder, and an organic material having a lower melting point than the binder.
- the first step and the second step are carried out by setting the temperature of the extrusion die 52 of the extrusion die 5 below the melting point of the binder and higher than the melting point of the organic material.
- the temperature of the extrusion die 52 of the extrusion die 5 is adjusted by the cooling device 55 and the heater 54, the temperature can be more reliably set to the target temperature.
- the mixture was kneaded at 135 ° C for 1 hour to obtain a kneaded product.
- Ethylene vinyl acetate copolymer (EVA) (melting point 84 ° C): 1.5wt% ⁇ organic material>
- Paraffin wax (melting point 55 ° C): 1.4 wt%
- DBP Dibutyl phthalate
- the obtained kneaded material was pulverized and classified into pellets having an average particle size of 3 mm.
- the pellets were extruded using the extruder shown in Fig. 1 under the following conditions, and cut.
- a cylindrical molded body (outer diameter ⁇ 22.5 mm, inner diameter 018.0 marauder, length 56 thighs) was obtained.
- an extrusion die of the extrusion molding machine an extrusion die for manufacturing a cylindrical molded body was used.
- Injection die inlet die temperature 140 ° C
- Extrusion die side die temperature 65 ° C
- the obtained molded body was decompressed at 1 ⁇ 10—3 Torr using a degreasing furnace. Degreasing was performed according to the temperature pattern shown in the graph of FIG.
- the temperature was kept at 300 ° C. for 3 hours, and in the second step, the temperature was kept at 500 ° C. for 1 hour.
- the obtained degreased body (molded body subjected to degreasing treatment) is sintered in an argon gas atmosphere at a temperature of 1350 ° C for 3 hours using a sintering furnace to obtain a cylindrical sintered body.
- Target dimensions metal products with an outer diameter of 20.0 marauders, an inner diameter of 16.0 mm, and a length of 50 marauders).
- Sintered body (Target dimensions: outer diameter ⁇ 20.0 mm, inner diameter 016.0 mm, length as in Example 1 except that the material of the kneaded material (pellet) was changed to the following material 50 bandits metal products).
- EVA Ethylene vinyl acetate copolymer
- cylindrical metal products (target dimensions: outer diameter 200.0 mm, inner diameter 016.0 mm) were manufactured by hot extrusion.
- the conditions for this hot extrusion were a temperature of 1100 ° C. and an extrusion pressure of 3 ton / cm 2 .
- Example 1 Error ⁇ 0.15%
- Examples 1 and 2 particularly the manufacturing method of Example 1, have high dimensional accuracy c.
- the manufacturing method of Comparative Example 1 has poor dimensional accuracy, and requires high temperature and high pressure.
- the facilities were dog-based.
- the method for manufacturing a sintered body according to the present invention has been described based on the embodiments, but the present invention is not limited to these.
- the method for manufacturing a sintered body of the present invention since a temperature gradient is provided in the extrusion die along the extrusion direction and extrusion is performed, metal sintering with high dimensional accuracy can be easily performed.
- the composition contains a metal powder, a binder, and an organic material having a lower melting point than the binder, it is possible to improve the formability at the time of extrusion molding and the degreasing at the time of degreasing. Thereby, the dimensional accuracy of the sintered metal product can be improved, and the manufacturing time of the sintered metal product can be shortened.
- the extrusion near the extrusion port of the extrusion die is performed at a temperature lower than the melting point of the binder and higher than the melting point of the organic material, the extrusion can be performed smoothly and reliably.
- the dimensional accuracy of the sintered product can be improved.
- the degreasing step includes a first step of degreasing in a low temperature range and a second step of degreasing in a higher temperature range than the first step, degreasing must be performed efficiently.
- the degreasing time can be reduced, the occurrence of degreasing defects such as cracks can be more reliably prevented, and the dimensional accuracy of the metal sintered product can be improved.
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Description
Claims
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE69927475T DE69927475T2 (de) | 1998-10-13 | 1999-10-08 | Verfahren zur herstellung gesinterter körper |
| EP99970345A EP1040887B1 (en) | 1998-10-13 | 1999-10-08 | Method of producing sintered body |
| US09/581,672 US6555051B1 (en) | 1998-10-13 | 1999-10-08 | Method for producing sintered body |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10/291210 | 1998-10-13 | ||
| JP29121098A JP4019522B2 (ja) | 1998-10-13 | 1998-10-13 | 焼結体の製造方法 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2000021703A1 true WO2000021703A1 (en) | 2000-04-20 |
Family
ID=17765898
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP1999/005599 Ceased WO2000021703A1 (en) | 1998-10-13 | 1999-10-08 | Method of producing sintered body |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US6555051B1 (ja) |
| EP (1) | EP1040887B1 (ja) |
| JP (1) | JP4019522B2 (ja) |
| KR (1) | KR100404527B1 (ja) |
| DE (1) | DE69927475T2 (ja) |
| WO (1) | WO2000021703A1 (ja) |
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| CN110919008A (zh) * | 2019-11-22 | 2020-03-27 | 东莞市豪准金属制品有限公司 | 一种金属注射成型工艺 |
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| US7691174B2 (en) * | 2004-03-08 | 2010-04-06 | Battelle Memorial Institute | Feedstock composition and method of using same for powder metallurgy forming a reactive metals |
| US20060024190A1 (en) * | 2004-07-27 | 2006-02-02 | General Electric Company | Preparation of filler-metal weld rod by injection molding of powder |
| US7387763B2 (en) * | 2004-07-27 | 2008-06-17 | General Electric Company | Preparation of sheet by injection molding of powder, consolidation, and heat treating |
| EP1808243B1 (en) * | 2004-10-15 | 2019-03-20 | Taisei Kogyo Co., Ltd. | Process for producing porous sinter, porous-sinter molding material, and porous sinter |
| NO326944B1 (no) * | 2006-11-20 | 2009-03-16 | Norsk Hydro As | Ekstruder for kontinuerlig ekstrudering av materialer med hoy viskositet |
| JP4702308B2 (ja) * | 2007-02-28 | 2011-06-15 | セイコーエプソン株式会社 | 焼結体の製造方法 |
| US7883662B2 (en) * | 2007-11-15 | 2011-02-08 | Viper Technologies | Metal injection molding methods and feedstocks |
| US8124187B2 (en) | 2009-09-08 | 2012-02-28 | Viper Technologies | Methods of forming porous coatings on substrates |
| DE102010050689A1 (de) | 2010-11-06 | 2012-05-10 | Schaeffler Technologies Gmbh & Co. Kg | Verfahren zur Herstellung eines keramischen Wälzkörpers |
| JP6246500B2 (ja) * | 2013-05-28 | 2017-12-13 | 日本電産サンキョー株式会社 | 希土類磁石の製造方法 |
| JP6390108B2 (ja) * | 2014-02-07 | 2018-09-19 | セイコーエプソン株式会社 | 焼結造形材料、焼結造形方法、焼結造形物および焼結造形装置 |
| CN104325144B (zh) * | 2014-10-27 | 2017-01-25 | 福立旺精密机电(中国)股份有限公司 | 一种金属注射成型催化脱脂方法以及催化脱脂炉 |
| KR101776616B1 (ko) * | 2015-10-02 | 2017-09-11 | 주식회사 쓰리디컨트롤즈 | 금속 분말 함유 원료를 이용한 3차원 프린팅 장치 |
| CN109500384A (zh) * | 2018-12-07 | 2019-03-22 | 东莞市华研新材料科技有限公司 | 基于金属粉末注射成型的手机框用外壳加工制作工艺 |
| CN110408897B (zh) * | 2019-08-13 | 2023-05-05 | 北京航大微纳科技有限公司 | 一种旋转靶材的垂直绑定装置以及绑定方法 |
| US20220410261A1 (en) * | 2019-12-04 | 2022-12-29 | Grundfos Holding A/S | A method of manufacturing a composite component with varying electric resistivity along a longitudinal direction |
| CN111468548B (zh) * | 2020-04-22 | 2023-01-24 | 永城职业学院 | 一种建筑金属材料用成型装置及其成型方法 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2787022A (en) | 1955-04-05 | 1957-04-02 | Dow Chemical Co | Extrusion apparatus |
| US3155502A (en) * | 1960-08-12 | 1964-11-03 | Union Carbide Corp | Powder metallurgy |
| US4457851A (en) * | 1981-12-29 | 1984-07-03 | Hitachi Metals, Ltd. | Ferrite magnet and method of producing same |
| JPS60221501A (ja) * | 1984-04-17 | 1985-11-06 | Honda Motor Co Ltd | 金属焼結体の製造方法 |
| JPH0686608B2 (ja) * | 1987-12-14 | 1994-11-02 | 川崎製鉄株式会社 | 金属粉末射出成形による鉄焼結体の製造方法 |
| CA2014974A1 (en) * | 1989-03-18 | 1991-10-19 | Ken Ikuma | Dies for extrusion moulding |
| EP0452580B1 (en) * | 1990-04-19 | 1999-06-23 | Seiko Epson Corporation | A resin bound magnet and its production process |
| EP0639417B1 (en) * | 1993-03-09 | 1998-12-09 | Citizen Watch Co. Ltd. | Process for manufacturing powder injection molded parts |
-
1998
- 1998-10-13 JP JP29121098A patent/JP4019522B2/ja not_active Expired - Fee Related
-
1999
- 1999-10-08 WO PCT/JP1999/005599 patent/WO2000021703A1/ja not_active Ceased
- 1999-10-08 KR KR10-2000-7006411A patent/KR100404527B1/ko not_active Expired - Fee Related
- 1999-10-08 US US09/581,672 patent/US6555051B1/en not_active Expired - Fee Related
- 1999-10-08 EP EP99970345A patent/EP1040887B1/en not_active Expired - Lifetime
- 1999-10-08 DE DE69927475T patent/DE69927475T2/de not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60216512A (ja) * | 1984-04-12 | 1985-10-30 | Seiko Epson Corp | 磁気ロ−ル用磁石 |
| JPH09148166A (ja) * | 1996-08-27 | 1997-06-06 | Seiko Epson Corp | 樹脂結合型磁石の製造方法 |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP1040887A4 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110919008A (zh) * | 2019-11-22 | 2020-03-27 | 东莞市豪准金属制品有限公司 | 一种金属注射成型工艺 |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1040887A4 (en) | 2001-12-19 |
| EP1040887A1 (en) | 2000-10-04 |
| EP1040887B1 (en) | 2005-09-28 |
| KR20010033052A (ko) | 2001-04-25 |
| JP2000119703A (ja) | 2000-04-25 |
| JP4019522B2 (ja) | 2007-12-12 |
| DE69927475D1 (de) | 2006-02-09 |
| DE69927475T2 (de) | 2006-06-22 |
| US6555051B1 (en) | 2003-04-29 |
| KR100404527B1 (ko) | 2003-11-05 |
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