The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Nov. 28, 2023

Filed:

Jun. 19, 2018
Applicants:

Posco Holdings Inc., Seoul, KR;

Research Institute of Industrial Science & Technology, Pohang-si, KR;

Posco Future M Co., Ltd., Pohang-si, KR;

Inventors:

Ki Sung You, Pohang-si, KR;

Hwang Yol Ryu, Pohang-si, KR;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C01D 5/08 (2006.01); B01J 19/24 (2006.01); C01C 1/18 (2006.01); C01C 1/24 (2006.01); H01M 4/04 (2006.01); H01M 4/58 (2010.01); H01M 10/054 (2010.01); H01M 4/02 (2006.01);
U.S. Cl.
CPC ...
C01D 5/08 (2013.01); B01J 19/24 (2013.01); C01C 1/185 (2013.01); C01C 1/24 (2013.01); H01M 4/0497 (2013.01); H01M 4/58 (2013.01); H01M 10/054 (2013.01); B01J 2219/00029 (2013.01); B01J 2219/00033 (2013.01); H01M 2004/028 (2013.01);
Abstract

A method for preparing a cathode active material precursor for a secondary battery, including: moving a co-precipitation filtrate generated after a co-precipitation reaction to a co-precipitation filtrate storage tank; removing a metal hydroxide by passing the co-precipitation filtrate through a filter; reacting the co-precipitation filtrate from which the metal hydroxide is removed with sulfuric acid or nitric acid to produce an ammonium sulfate or an ammonium nitrate while removing ammonia from the co-precipitation filtrate from which the metal hydroxide is removed; cooling and crystallizing the co-precipitation filtrate from which the metal hydroxide and ammonia are removed to precipitate a sodium sulfate; filtering the precipitated sodium sulfate to separate the precipitated sodium sulfate from the co-precipitation filtrate from which the metal hydroxide and ammonia are removed; drying the sodium sulfate separated from the co-precipitation filtrate and moving the co-precipitation filtrate separated from the sodium sulfate to a circulation concentration tank; and heating the co-precipitation filtrate stored in the circulation concentration tank to a predetermined temperature for recycling and performing Npurging or bubbling, is provided.


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