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:
Jun. 27, 2017

Filed:

Oct. 25, 2013
Applicant:

Chiyoda Corporation, Yokohama-shi, JP;

Inventors:

Kazushige Kawamura, Yokohama, JP;

Dai Takeda, Yokohama, JP;

Eiji Awai, Yokohama, JP;

Noboru Takei, Yokohama, JP;

Masataka Uemura, Yokohama, JP;

Assignee:

Chiyoda Corporation, Yokohama-shi, JP;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 17/74 (2006.01); C01B 17/76 (2006.01); C01B 17/80 (2006.01); B01D 53/86 (2006.01); B01D 53/50 (2006.01); B01D 53/75 (2006.01); C02F 1/72 (2006.01); C02F 1/78 (2006.01); B01D 53/14 (2006.01); C02F 1/28 (2006.01); C02F 101/10 (2006.01); C02F 103/18 (2006.01);
U.S. Cl.
CPC ...
B01D 53/8609 (2013.01); B01D 53/507 (2013.01); B01D 53/75 (2013.01); C01B 17/74 (2013.01); B01D 53/1481 (2013.01); B01D 2252/2056 (2013.01); B01D 2255/702 (2013.01); C02F 1/283 (2013.01); C02F 1/72 (2013.01); C02F 1/78 (2013.01); C02F 2101/101 (2013.01); C02F 2103/18 (2013.01);
Abstract

This desulfurization device is for desulfurizing a discharge gas which contains sulfur oxides and which was discharged from a device for sulfuric acid production that includes a concentrated-sulfuric-acid production step in which sulfur trioxide gas obtained by oxidizing sulfur dioxide gas is absorbed in an aqueous sulfuric acid solution while supplying water thereto to thereby produce sulfuric acid having a concentration as high as 90 wt % or more but less than 99 wt %, the desulfurization device comprising: a desulfurization tower in which the sulfur oxides are removed from the discharge gas and, simultaneously therewith, dilute sulfuric acid is formed from the sulfur oxides; and a dilute sulfuric acid mixer which, in the concentrated-sulfuric-acid production step, mixes the dilute sulfuric acid with the aqueous sulfuric acid solution.


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