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:
Oct. 05, 2021

Filed:

Nov. 01, 2016
Applicant:

Korea Institute of Machinery & Materials, Daejeon, KR;

Inventors:

Dae-hoon Lee, Daejeon, KR;

Younghoon Song, Daejeon, KR;

Kwan-Tae Kim, Daejeon, KR;

Sungkwon Jo, Daejeon, KR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/86 (2006.01); B01D 53/56 (2006.01); B01D 53/62 (2006.01); B01D 53/96 (2006.01); B01J 38/10 (2006.01); B01D 53/32 (2006.01); C01B 3/02 (2006.01); B01J 38/04 (2006.01); C01B 13/10 (2006.01); C01B 3/36 (2006.01); C01B 3/38 (2006.01);
U.S. Cl.
CPC ...
B01D 53/8628 (2013.01); B01D 53/32 (2013.01); B01D 53/56 (2013.01); B01D 53/62 (2013.01); B01D 53/864 (2013.01); B01D 53/8625 (2013.01); B01D 53/96 (2013.01); B01J 38/04 (2013.01); B01J 38/10 (2013.01); C01B 3/02 (2013.01); C01B 3/36 (2013.01); C01B 3/38 (2013.01); C01B 13/10 (2013.01); B01D 2256/20 (2013.01); B01D 2256/22 (2013.01); B01D 2257/402 (2013.01); B01D 2257/404 (2013.01); B01D 2259/818 (2013.01); C01B 2203/025 (2013.01); C01B 2203/0465 (2013.01); C01B 2203/0861 (2013.01); Y02P 20/584 (2015.11);
Abstract

A process discharge gas polluted material removal device with a regenerating means of a polluted oxidation catalyst includes: an oxidation catalyst tower connected to a pipe circulating a process discharge gas including a combustible material, an organic material, an inorganic material, and nitrogen oxide and having a first temperature and having an oxidation catalyst embedded therein, the oxidation catalyst oxidizing and removing the combustible material; and a plasma reactor connected to the oxidation catalyst tower in front of the oxidation catalyst, generating a synthesis gas including hydrogen and having a high temperature of 300° C. or more by a plasma reaction, and supplying the synthesis gas including the hydrogen to the oxidation catalyst to regenerate the oxidation catalyst poisoned by the organic material and the inorganic material.


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