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US5853451A Expired / Lapsed US ⏱️ 0.0 years remaining

Ultrafine spherical nickel powder for use as an electrode of laminated ceramic capacitors

Assignee: JFE Steel Corp
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Filing: 1995-10-02
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Granted: 1998-12-29
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Expires: 2015-10-02
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Abstract

Abstract Ultrafine spherical nickel powder for use in a laminate ceramics capacitor is produced through a process employing a vapor phase chemical reaction between nickel chloride and hydrogen. The process includes the steps of: i) charging a reaction vessel with nickel chloride and evaporating the nickel chloride to generate vapor of nickel chloride; ii) mixing an inert gas with the vapor of the nickel chloride to form a mixture gas having a nickel chloride gas concentration of 0.05 to 0.3, and sending the mixture gas to a reaction zone; iii) bringing, in the reaction zone, the mixture gas into contact and mixing with hydrogen which is supplied from a nozzle at a temperature of 1004° C. to 1453° C., in such a manner that the flow rate ratio of the hydrogen to the mixture gas meets the condition of (H 2 /(NiCl 2 +inert gas)) <1, thereby causing the chemical reaction; and iv) cooling the generated ultrafine nickel powder together with the gas and collecting the ultrafine nickel powder.

Inventors

  • 👤 Hiroyuki Ishikawa

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 03:04
CPC Classifications
B; B22; B22F; B22F9/00; B22F9/16; B22F9/18; B22F9/28; B22F2999/00; Y; Y10; Y10S; Y10S75/00; Y10S75/953

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 210 words
A process for producing ultrafine spherical nickel powder for use in a laminate ceramics capacitor through a vapor phase chemical reaction between nickel chloride and hydrogen, said process comprising the steps of: i) charging a reaction vessel with said nickel chloride and evaporating said nickel chloride to generate vapor of nickel chloride; ii) mixing an inert gas with said vapor of the nickel chloride to form a mixture gas having a nickel chloride gas concentration of about 0.05 to about 0.3, and sending said mixture gas to a reaction zone; iii) bringing, in said reaction zone, said mixture gas into contact and mixing with hydrogen which is supplied from a nozzle at a temperature of about 1004° C. to about 1453° C. at a flow rate of said mixture gas which is decreased by keeping the amount of hydrogen supplied low, such that a flow rate ratio of said hydrogen to said mixture gas meets the condition of (H 2 /(NiCl 2 +inert gas)) ≦1, thereby causing said vapor phase chemical reaction; iv) generating ultrafine spherical nickel powder having a particle size of 0.2 to 3 μm by said chemical reaction; and v) cooling the generated ultrafine nickel powder together with the mixture gas and collecting said ultrafine nickel powder.
Claim 2
Dependent Claim 210 words
A process for producing ultrafine spherical nickel powder for use in a laminate ceramics capacitor through a vapor phase chemical reaction between nickel chloride and hydrogen, said process comprising the steps of: i) charging a reaction vessel with said nickel chloride and evaporating said nickel chloride to generate vapor of nickel chloride; ii) mixing an inert gas with said vapor of the nickel chloride to form a mixture gas having a nickel chloride gas concentration of about 0.05 to about 0.3, and sending said mixture gas to a reaction zone; iii) bringing, in said reaction zone, said mixture gas into contact and mixing with hydrogen which is supplied from a nozzle at a temperature of about 1004° C. to about 1453° C. at a flow rate of said mixture gas which is decreased by keeping the amount of hydrogen supplied low, such that a flow rate ratio of said hydrogen to said mixture gas meets the condition of (H 2 /(NiCl 2 +inert gas)) ≦1, thereby causing said vapor phase chemical reaction; iv) generating ultrafine spherical nickel powder having a particle size of 0.2 to 3 μm by said chemical reaction; and v) cooling the generated ultrafine nickel powder together with the mixture gas and collecting said ultrafine nickel powder.
Claim 3
Dependent Claim 29 words
A process for producing ultrafine spherical nickel powder according to claim 1, wherein the concentration of said vapor of nickel chloride in said mixture gas is 0.06 to 0.15.
Claim 4
Dependent Claim 25 words
A process for producing ultrafine spherical nickel powder according to claim 1, wherein the temperature in said reaction zone is 1010° C. to 1100° C.
Claim 5
Dependent Claim 35 words
A process for producing ultrafine spherical nickel powder according to claim 1, wherein the flow rate ratio of said hydrogen to said mixture gas meets the condition of 0.3≦H 2 /(NiCl 2 +inert gas) ≦0.6.
Claim 6
Dependent Claim 26 words
A process for producing ultrafine spherical nickel powder according to claim 1, wherein said inert gas is selected from the group consisting of argon and nitrogen.

References Cited (Backward Citations)

US4383852A Cited
US4810285A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 2001-12-28 2002-06-29 2002-12-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2005-12-28 2006-06-29 2006-12-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2009-12-28 2010-06-29 2010-12-29 $7700.00 Window Closed / Lapsed

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