Nickel hydroxide composite material for alkaline rechargeable battery

Patent metadata

Field	Value
Publication number	US-2017194634-A1
Application number	US-201615370756-A
Country	US
Kind code	A1
Filing date	Dec 6, 2016
Priority date	Jan 5, 2016
Publication date	Jul 6, 2017
Grant date	—

Abstract

Provided are uniquely structured electrochemically active particles characterized by a first electrochemically active material and a second electrochemically active material disposed about the first material whereby at least the second material includes a modifier present as a continuous transition concentration gradient from the first material into the second material whereby the concentration is lower in the first material than the second material. Also provided are processes of producing the particle and electrochemical cells incorporating the particles as a positive electrode material in a cathode.

First claim

1 . An electrochemically active particle comprising:
a first electrochemically active material; and a second electrochemically active material disposed about the first electrochemically active material, the second electrochemically active material comprising single element modifier, the modifier present as a continuous transition concentration gradient from said first electrochemically active material into said second electrochemically active material, and the modifier concentration being lower in the first electrochemically active material than in the second electrochemically active material, and wherein the atomic percentage of constituent elements excluding the modifier of the first electrochemically active material and the second electrochemically active material differ by less than 20 atomic percent.

2 . The electrochemically active particle of claim 1 wherein the modifier is a metallic element, the metallic element different from all of said constituent elements.

3 . The electrochemically active particle of claim 1 wherein metallic constituents of the first electrochemically active material and the second electrochemically active material are identical other than the presence of the modifier.

4 . The electrochemically active particle of claim 1 wherein the modifier is selected from the group consisting of Al, Ba, Bi, Ca, Co, Cr, Cu, F, Fe, In, K, La, Li, Mg, Mn, Na, Nd, Pb, Pr, Ru, Sb, Sc, Se, Sn, Sr, Te, Ti, Y and Zn.

5 . The electrochemically active particle of claim 1 wherein the first electrochemically active material and the second electrochemically active material comprise nickel as a metallic predominant.

6 . The electrochemically active particle of claim 1 wherein the atomic ratio of modifier at the surface of the particle relative to the first electrochemically active material is from about 10:1 to about 1.2:1.

7 . The electrochemically active particle of claim 1 wherein the first electrochemically active material and the second electrochemically active material comprise the constituent elements nickel and cobalt.

8 . The electrochemically active particle of claim 1 wherein the particle has a BET surface area of 40 m 2 /g or greater.

9 . The electrochemically active particle of claim 1 wherein the second electrochemically active material comprises a plurality of surface pores extending from an outer most portion of the second electrochemically active material toward the first electrochemically active material.

10 . The electrochemically active particle of claim 9 wherein the plurality of surface pores have an average pore diameter of less than 35 angstroms, optionally less than 25 angstroms.

11 . The electrochemically active particle of claim 9 wherein the plurality of surface pores has a pore volume of 0.02 cc/g or greater, optionally 0.025 cc/g or greater.

12 . The electrochemically active particle of claim 9 wherein the percentage of pores with an area of 15 angstroms or less is 5 percent or greater.

13 . A process of forming an electrochemically active particle in a single tank reactor comprising:
simultaneously combining one or more metal salts with a conductive modifier and a solvent in a single reactor to form a combination, the modifier having a solubility lower than the metal salts in the solvent; agitating the combination; and adding a base to the combination to precipitate the electrochemically active particle.

14 . The process of claim 13 wherein the pH is maintained at 9.0 to 10.7.

15 . The process of claim 13 wherein the step of maintaining is by adding the base at a constant rate.

16 . The process claim 15 wherein the base is NaOH or KOH.

17 . The process of claim 15 wherein the base is added from a solution of 15% to 25% and at a rate of 3 cc/min or less.

18 . The process of claim 13 further comprising adding ammonia to the reactor, the ammonia added at a molar ratio to salt of less than 7, optionally less than 2.

19 . The process of claim 13 further comprising maintaining the temperature at 20° C. to 100° C.

20 . The process of claim 13 wherein the metal salt and the conductive modifier are added to the reactor in from a single feed stream.

Assignees

• Basf Corp

Inventors

• Young Kwo
• Mays William C
• Wang Lixin

Classifications

• C01P2006/11

  Powder tap density · CPC title

• C01P2004/04

  obtained by TEM, STEM, STM or AFM · CPC title

• H01M4/626

  Metals · CPC title

• H01M4/32 Primary

  Nickel oxide or hydroxide electrodes · CPC title

• H01M4/52

  of nickel, cobalt or iron · CPC title