Production method of electrode catalyst, electrode catalyst, composition for forming gas diffusion electrode, gas diffusion electrode, membrane-electrode assembly (MEA), and fuel cell stack

Patent metadata

Field	Value
Publication number	US-9437876-B2
Application number	US-201515022753-A
Country	US
Kind code	B2
Filing date	Mar 27, 2015
Priority date	Mar 28, 2014
Publication date	Sep 6, 2016
Grant date	Sep 6, 2016

Abstract

Provided is a production method of an electrode catalyst that can reduce the content of chlorine species reliably and sufficiently through a simple operation, even when using an electrode catalyst precursor containing a high concentration of chlorine (Cl) species as a raw material of the electrode catalyst. The production method of the electrode catalyst has a core-shell structure including a core part formed on a support and a shell part formed to cover at least a part of a surface of the core part. The production method includes a first step (1) of preparing a first liquid with an electrode catalyst precursor (I) being dispersed in ultrapure water by adding the electrode catalyst precursor (I) to the ultrapure water, the electrode catalyst precursor (I) being produced using a material containing chlorine (Cl) species, and exhibiting a chlorine (Cl) species concentration not lower than a first chlorine (Cl) species concentration when measured by X-ray fluorescence (XRF) spectroscopy; and a second step (2) of preparing a second liquid by dispersing an electrode catalyst precursor (II), the electrode catalyst precursor (II) being obtained by filtrating and washing the electrode catalyst precursor (I) contained in the first liquid with ultrapure water, and then performing washing until an electric conductivity ρ of a filtrate has become a first value or lower.

First claim

The invention claimed is:

1. A production method of an electrode catalyst having a core-shell structure including a support, a core part formed on said support and a shell part formed to cover at least a part of a surface of said core part, comprising:
a first step (1) of preparing a first liquid with an electrode catalyst precursor (I) being dispersed in ultrapure water by adding said electrode catalyst precursor (I) to the ultrapure water, said electrode catalyst precursor (I) being produced using a material containing chlorine (Cl) species, and exhibiting a chlorine (Cl) species concentration not lower than a predetermined first chlorine (Cl) species concentration when measured by X-ray fluorescence (XRF) spectroscopy; and
a second step (2) of preparing a second liquid by dispersing an electrode catalyst precursor (II) in ultrapure water, said electrode catalyst precursor (II) being obtained by filtrating and washing said electrode catalyst precursor (I) contained in said first liquid with ultrapure water, and then repeatedly performing washing until an electric conductivity ρ of a filtrate obtained after washing has become a first predetermined value or lower when measured by a JIS-standard testing method (JIS K0552).

2. The production method of the electrode catalyst according to claim 1 , wherein said first chlorine (Cl) species concentration is 6,000 ppm.

3. The production method of the electrode catalyst according to claim 1 , wherein said first predetermined value is a value selected from a range of not higher than 100 μS/cm.

4. The production method of the electrode catalyst according to claim 1 , wherein said electrode catalyst precursor (I) used in said first step is subjected to a pretreatment process comprising:
a step (P1) of preparing a P1 liquid with an electrode catalyst precursor (PI) being dispersed in ultrapure water by adding said electrode catalyst precursor (PI) to the ultrapure water, said electrode catalyst precursor (PI) being produced using a material containing chlorine (Cl) species, and exhibiting a chlorine (Cl) species concentration not lower than a predetermined second chlorine (Cl) species concentration when measured by X-ray fluorescence (XRF) spectroscopy;
a step (P2) of preparing a P2 liquid by dispersing an electrode catalyst precursor (PII) in ultrapure water, said electrode catalyst precursor (PII) being obtained by filtrating and washing said electrode catalyst precursor (PI) contained in said P1 liquid with ultrapure water, and then repeatedly performing washing until an electric conductivity ρ of a filtrate obtained after washing has become a predetermined value of the step P1 or lower when measured by the JIS-standard testing method (JIS K0552); and
a step (P3) of drying said P2 liquid.

5. The production method of the electrode catalyst according to claim 4 , wherein said second chlorine (Cl) species concentration is 6,000 ppm.

6. The production method of the electrode catalyst according to claim 4 , wherein said predetermined value of the step P1 is a value selected from the range of not higher than 100 μS/cm.

7. The production method of the electrode catalyst according to claim 1 , further comprising a third step (3) of drying said second liquid obtained after said second step.

8. The production method of the electrode catalyst according to claim 7 , further comprising a fourth step (4) of preparing a third liquid with said electrode catalyst precursor (II) being dispersed in ultrapure water, by adding said electrode catalyst precursor (II) obtained after said third step (3) to the ultrapure water.

9. The production method of the electrode catalyst according to claim 8 , further comprising:
a fifth step (5) of preparing, after said fourth step (4),
a fourth liquid with an electrode catalyst precursor (IV) being dispersed in ultrapure water, said electrode catalyst precursor (IV) being obtained by filtrating and washing an electrode catalyst precursor (III) contained in said third liquid with ultrapure water of a temperature of 60° C. to a boiling point thereof, and then repeatedly performing washing until an electric conductivity ρ of a filtrate obtained after washing has become a second predetermined value or lower; and
a sixth step (6) of drying said fourth liquid.

10. The production method of the electrode catalyst according to claim 9 , wherein said second predetermined value is a value selected from the range of not higher than 100 μS/cm.

11. The production method of the electrode catalyst according to claim 9 , further comprising a seventh step (7) established between said fifth step (5) and said drying step (6), said seventh step (7) allowing said fourth liquid to be retained under at least one stage of a temperature predetermined within a range of 60° C. to a boiling point thereof for a predetermined retention time.

12. The production method of the electrode catalyst according to claim 1 , further comprising a first step′ (1′) established before said first step, said first step′ (1′) allowing an electrode catalyst precursor (I0) to be dispersed in an aqueous solution obtained by adding to ultrapure water at least one kind of acid selected from the group consisting of a sulfuric acid and a nitric acid, and then retained under at least one stage of a temperature predetermined within a range of 10 to 95° C. for a predetermined retention time.

13. The production method of the electrode catalyst according to claim 1 , wherein said shell part contains at least one metal selected from platinum (Pt) and a platinum (Pt) alloy, and said core part contains at least one metal selected from the group consisting of palladium (Pd), a palladium (Pd) alloy, a platinum (Pt) alloy, gold (Au), nickel (Ni) and a nickel (Ni) alloy.

14. The production method of the electrode catalyst according to claim 13 , wherein a platinum (Pt) chloride is used as a raw material of a metal constituting said shell part.

15. The production method of the electrode catalyst according to claim 1 , wherein said shell part has:
a first shell part formed to cover at least a part of the surface of said core part; and
a second shell part formed to cover at least a part of a surface of said first shell part.

16. The production method of the electrode catalyst according to claim 15 , wherein a platinum (Pt) chloride is used as a raw material of a metal constituting said second shell part.

17. The production method of the electrode catalyst according to claim 1 , further comprising a third step (3) of drying said second liquid obtained after said second step, wherein said electrode catalyst precursor (I) used in said first step is subjected to a pretreatment process comprising:
a step (P1) of preparing a P1 liquid with an electrode catalyst precursor (PI) being dispersed in ultrapure water by adding said electrode catalyst precursor (PI) to the ultrapure water, said electrode catalyst precursor (PI) being produced using a material containing chlorine (Cl) species, and exhibiting a chlorine (Cl) species concentration not lower than a predetermined second chlorine (Cl) species concentration when measured by X-ray fluorescence (XRF) spectroscopy;
a step (P2) of preparing a P2 liquid by dispersing an electrode catalyst precursor (PII) in ultrapure water, said electrode catalyst precursor (PII) being obtained by filtrating and washing said electrode catalyst precursor (PI) contained in said P1 liquid with ultrapure water, and then repeatedly performing washing until an electric conductivity ρ of a filtrate obtained after washing has become a predetermined value of the step P1 or

Assignees

• N E Chemcat Corp

Inventors

• Nakamura Yoko
• Nagamori Kiyotaka
• Mizusaki Tomoteru
• Tsubaki Takuya

Classifications

• H01M4/8825

  Methods for deposition of the catalytic active composition · CPC title

• H01M4/926

  on carbon or graphite · CPC title

• H01M4/8657 Primary

  layered · CPC title

• H01M4/921

  Alloys or mixtures with metallic elements · CPC title

• Y02P70/50

  Manufacturing or production processes characterised by the final manufactured product · CPC title