IP Library Granted Patent US 10,351,438
Granted Patent B2
US 10,351,438 · App. 15/539,302 · Granted Jul 16, 2019

Stannous oxide powder and method for producing stannous oxide powder

Inventors: Hirotaka Hirano (Sanda, JP); Takuma Katase (Sanda, JP)
Assignee: MITSUBISHI MATERIALS CORPORATION
C01G19/02C01P2004/03C01P2004/51C01P2004/61C01P2006/11C01P2006/12C01P2006/80
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Quick Facts
Patent No.
US 10,351,438
App. No.
15/539,302
Granted
Jul 16, 2019
Kind
B2
Abstract

A stannous oxide powder which has a high dissolution rate into various acid solutions such as a plating solution and is particularly suitable as a Sn supply material to a plating solution, and a method for producing the stannous oxide powder are provided. The stannous oxide powder is a particle body having a plurality of plate-like protrusions protruding outward, and has an average particle size in a range of 1 μm to 15 μm.

Claims (57)

1. A stannous oxide powder which is a particle body having a plurality of plate-like protrusions protruding outward, and has an average particle size in a range of 1 μm to 15 μm, wherein the amount of alkali is 10 ppm by mass or less, and the amount of acid excluding carbonic acid is 50 ppm by mass or less.

2. The stannous oxide powder according to claim 1 ,

wherein a specific surface area of the stannous oxide powder is 1.0 m 2 /g or more.

3. The stannous oxide powder according to claim 1 ,

wherein a bulk density of the stannous oxide powder is in a range of 1.5 g/cm 3 or more and less than 2.0 g/cm 3 .

4. A stannous oxide powder which is a particle body having a plurality of plate-like protrusions protruding outward, and has an average particle size in a range of 1 μm to 15 μm, further comprising:

0.2 mass % or more of carbonic acid.

5. A method for producing a stannous oxide powder, wherein the stannous oxide powder is a particle body having a plurality of plate-like protrusions protruding outward, and has an average particle size in a range of 1 μm to 15 μm, the method comprising:

an Sn ion-containing acid solution forming step of causing Sn ions to be contained in an acid solution, thereby obtaining an Sn ion-containing acid solution;

a first neutralization step of adding an alkaline solution of any one or more selected from ammonium carbonate, ammonium bicarbonate, and ammonia water to the Sn ion-containing acid solution to maintain a pH of 3 to 6, thereby obtaining a Sn precipitate;

a Sn precipitate separation step of separating the Sn precipitate from the Sn ion-containing acid solution;

a Sn precipitate dispersion step of dispersing the separated Sn precipitate in a solvent; and

a second neutralization step of maintaining the dispersion liquid of the Sn precipitate at 50° C. or lower, and adding an alkaline solution thereto for 1 hour or longer to achieve a pH of 6 to 12, thereby obtaining SnO from the Sn precipitate.

6. The stannous oxide powder according to claim 2 ,

wherein a bulk density of the stannous oxide powder is in a range of 1.5 g/cm 3 or more and less than 2.0 g/cm 3 .

7. The stannous oxide powder according to claim 4 ,

wherein a specific surface area of the stannous oxide powder is 1.0 m 2 /g or more.

8. The stannous oxide powder according to claim 4 ,

wherein a bulk density of the stannous oxide powder is in a range of 1.5 g/cm 3 or more and less than 2.0 g/cm 3 .

9. The stannous oxide powder according to claim 4 ,

wherein the amount of alkali is 10 ppm by mass or less, and the amount of acid excluding carbonic acid is 50 ppm by mass or less.

10. The stannous oxide powder according to claim 4 ,

wherein

a specific surface area of the stannous oxide powder is 1.0 m 2 /g or more, and

a bulk density of the stannous oxide powder is in a range of 1.5 g/cm 3 or more and less than 2.0 g/cm 3 .

11. The stannous oxide powder according to claim 4 ,

wherein,

a specific surface area of the stannous oxide powder is 1.0 m 2 /g or more, and

the amount of alkali is 10 ppm by mass or less, and the amount of acid excluding carbonic acid is 50 ppm by mass or less.

12. The stannous oxide powder according to claim 4 ,

wherein

a bulk density of the stannous oxide powder is in a range of 1.5 g/cm 3 or more and less than 2.0 g/cm 3 , and

the amount of alkali is 10 ppm by mass or less, and the amount of acid excluding carbonic acid is 50 ppm by mass or less.

13. A method for producing the stannous oxide powder according to claim 1 , the method comprising:

an Sn ion-containing acid solution forming step of causing Sn ions to be contained in an acid solution, thereby obtaining an Sn ion-containing acid solution;

a first neutralization step of adding an alkaline solution of any one or more selected from ammonium carbonate, ammonium bicarbonate, and ammonia water to the Sn ion-containing acid solution to maintain a pH of 3 to 6, thereby obtaining a Sn precipitate;

a Sn precipitate separation step of separating the Sn precipitate from the Sn ion-containing acid solution;

a Sn precipitate dispersion step of dispersing the separated Sn precipitate in a solvent; and

a second neutralization step of maintaining the dispersion liquid of the Sn precipitate at 50° C. or lower, and adding an alkaline solution thereto for 1 hour or longer to achieve a pH of 6 to 12, thereby obtaining SnO from the Sn precipitate.

14. A method for producing the stannous oxide powder according to claim 2 , the method comprising:

an Sn ion-containing acid solution forming step of causing Sn ions to be contained in an acid solution, thereby obtaining an Sn ion-containing acid solution;

a first neutralization step of adding an alkaline solution of any one or more selected from ammonium carbonate, ammonium bicarbonate, and ammonia water to the Sn ion-containing acid solution to maintain a pH of 3 to 6, thereby obtaining a Sn precipitate;

a Sn precipitate separation step of separating the Sn precipitate from the Sn ion-containing acid solution;

a Sn precipitate dispersion step of dispersing the separated Sn precipitate in a solvent; and

a second neutralization step of maintaining the dispersion liquid of the Sn precipitate at 50° C. or lower, and adding an alkaline solution thereto for 1 hour or longer to achieve a pH of 6 to 12, thereby obtaining SnO from the Sn precipitate.

15. A method for producing the stannous oxide powder according to claim 3 , the method comprising:

an Sn ion-containing acid solution forming step of causing Sn ions to be contained in an acid solution, thereby obtaining an Sn ion-containing acid solution;

a first neutralization step of adding an alkaline solution of any one or more selected from ammonium carbonate, ammonium bicarbonate, and ammonia water to the Sn ion-containing acid solution to maintain a pH of 3 to 6, thereby obtaining a Sn precipitate;

a Sn precipitate separation step of separating the Sn precipitate from the Sn ion-containing acid solution;

a Sn precipitate dispersion step of dispersing the separated Sn precipitate in a solvent; and

a second neutralization step of maintaining the dispersion liquid of the Sn precipitate at 50° C. or lower, and adding an alkaline solution thereto for 1 hour or longer to achieve a pH of 6 to 12, thereby obtaining SnO from the Sn precipitate.

16. A method for producing the stannous oxide powder according to claim 4 , the method comprising:

an Sn ion-containing acid solution forming step of causing Sn ions to be contained in an acid solution, thereby obtaining an Sn ion-containing acid solution;

a first neutralization step of adding an alkaline solution of any one or more selected from ammonium carbonate, ammonium bicarbonate, and ammonia water to the Sn ion-containing acid solution to maintain a pH of 3 to 6, thereby obtaining a Sn precipitate;

a Sn precipitate separation step of separating the Sn precipitate from the Sn ion-containing acid solution;

a Sn precipitate dispersion step of dispersing the separated Sn precipitate in a solvent; and

a second neutralization step of maintaining the dispersion liquid of the Sn precipitate at 50° C. or lower, and adding an alkaline solution thereto for 1 hour or longer to achieve a pH of 6 to 12, thereby obtaining SnO from the Sn precipitate.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 23, 2017
From: HIRANO, HIROTAKA; KATASE, TAKUMA
To: MITSUBISHI MATERIALS CORPORATION
Reel/Frame 042795/0724 →
Priority Claims (2)
JP 2015-027867 · Feb 16, 2015 · national
JP 2016-010755 · Jan 22, 2016 · national
Continuity (1)
Related Publication 20180327274A1 · Nov 15, 2018