Method for manufacturing spherical metal powder
Abstract
An embodiment of the present invention provides a method for manufacturing spherical metal powder, comprising the steps of: (a) forming a slurry by mixing ultra-fine raw metal with a binder and a solvent; (b) forming granular powders by granulating the slurry through spray drying; (c) adding a separating agent to prevent sintering between the granular powders; (d) forming spherical metal powder by continuously degreasing and sintering the granular powders; (e) adding a deoxidizer for high purity of the sintered spherical metal powder to carry out deoxidation treatment; and (f) removing the separating agent and an oxide from the deoxidized spherical metal powder.
Claims
exact text as granted — not AI-modified1 . A method of preparing spherical metal powder, comprising:
(a) mixing an ultra-fine raw metal with a binder and a solvent to form a slurry; (b) granulating the slurry through spray drying to form granular powder; (c) adding a separating agent to prevent sintering between granular powder particles; (d) continuously performing degreasing and sintering on the granular powder to form spherical metal powder; (e) performing deoxidation treatment by adding a deoxidizer to achieve high purity of the sintered spherical metal powder; and (f) removing the separating agent and oxide from the deoxidized spherical metal powder.
2 . The method of claim 1 , wherein the spherical metal powder is selected from the group consisting of CP—Ti-based alloys, Ti—Al-based alloys, Ti—Al—V-based alloys, and a combination thereof.
3 . The method of claim 1 , wherein a particle size range of the spherical metal powder is 1 to 300 μm.
4 . The method of claim 1 , wherein the ultra-fine raw metal is one or more selected from the group consisting of titanium hydride, titanium, aluminum, vanadium, tin, palladium, nickel, molybdenum, chromium, cobalt, zirconium, zirconium hydride, niobium, and a combination thereof.
5 . The method of claim 1 , wherein the ultra-fine raw metal is prepared from a raw material selected from the group consisting of titanium sponge, titanium scrap, and a combination thereof.
6 . The method of claim 1 , wherein in step (a), the solvent includes water and ethyl alcohol, the binder includes a polyvinyl pyrrolidone (PVP) binder, which are physically mixed using a mixing device.
7 . The method of claim 6 , wherein in step (a), 100 to 500 ml of ethyl alcohol, 50 to 650 g of an ultra-fine raw metal, and 16 to 150 ml of PVP are mixed with respect to 1 L of water.
8 . The method of claim 1 , wherein in step (b), the spray drying is performed by intermittently spraying the slurry at a pneumatic pressure of 2 to 8 kg/cm 2 in a chamber maintained at a vacuum of 10 −1 torr or less to form granular powder.
9 . The method of claim 1 , wherein a particle size range of the granular powder is 1 to 350 μm.
10 . The method of claim 9 , wherein in step (b), the granular powder that is outside the particle size range after granulation is re-granulated.
11 . The method of claim 1 , wherein in step (c), the separating agent includes MgO powder, K 2 O powder, or a mixture thereof.
12 . The method of claim 1 , wherein in step (d), a degreasing initial vacuum degree is 10 −6 to 10 −2 torr.
13 . The method of claim 1 , wherein in step (d), a degreasing temperature is 100 to 500° C., and a temperature increase rate consists of two stages of 2 to 8° C./min and 9 to 20° C./min.
14 . The method of claim 1 , wherein in step (d), a sintering temperature is 600° C. to 1500° C.
15 . The method of claim 14 , wherein in step (d), a sintering temperature increase rate consists of two stages of 2 to 8° C./min and 9 to 20° C./min, and a sintering holding time is 1 min to 50 h.
16 . The method of claim 1 , wherein in step (d), sintering is performed until pores inside the granular powder is controlled to 10% or less.
17 . The method of claim 1 , wherein in step (d), sintering is performed until pores inside the granular powder is controlled to 5% or less.
18 . The method of claim 1 , wherein in step (e), the deoxidizer is Ca gas, Mg gas, or a combination thereof.
19 . The method of claim 1 , wherein in step (e), a deoxidation initial vacuum degree is 10 −6 to 10 −2 torr.
20 . The method of claim 1 , wherein in step (e), a deoxidation temperature is 800 to 1100° C.
21 . The method of claim 20 , wherein a deoxidation temperature increase rate is 5 to 10° C./min, and a deoxidation holding time after the temperature increase is 1 to 5 h.
22 . The method of claim 1 , wherein in step (f), the deoxidized spherical metal powder is pickled and washed with water in dilute hydrochloric acid, dilute sulfuric acid, or a mixture thereof to remove remaining oxides.
23 . The method of claim 1 , wherein in step (f), the spherical metal powder from which the separating agent and oxide have been removed is dried at 50 to 150° C.
24 . The method of claim 23 , wherein in step (f), a drying time is 1 min to 5 h.Join the waitlist — get patent alerts
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