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. 11, 2014

Filed:

Sep. 05, 2008
Applicants:

John Buschmann, Knoxville, TN (US);

Lawrence Joseph Czarnecki, Knoxville, TN (US);

Mou Jian, Knoxville, TN (US);

Frederic Zenon Kozak, Knoxville, TN (US);

Inventors:

John Buschmann, Knoxville, TN (US);

Lawrence Joseph Czarnecki, Knoxville, TN (US);

Mou Jian, Knoxville, TN (US);

Frederic Zenon Kozak, Knoxville, TN (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/60 (2006.01); B01J 23/92 (2006.01); F23J 15/00 (2006.01); F23J 15/04 (2006.01); B01D 53/86 (2006.01); B03C 3/017 (2006.01); B01D 53/96 (2006.01); B01D 53/50 (2006.01); B01D 53/77 (2006.01);
U.S. Cl.
CPC ...
B01D 53/8631 (2013.01); B01J 23/92 (2013.01); F23J 15/006 (2013.01); B01D 2255/9207 (2013.01); B01D 2251/2062 (2013.01); B01D 2251/2067 (2013.01); F23J 2215/10 (2013.01); F23J 15/04 (2013.01); B01D 53/505 (2013.01); F23J 2215/20 (2013.01); B01D 2251/404 (2013.01); B01D 2251/604 (2013.01); B01D 53/8637 (2013.01); B03C 3/017 (2013.01); B01D 2255/9045 (2013.01); B01D 2255/20776 (2013.01); B01D 2255/20707 (2013.01); F23J 2217/102 (2013.01); F23J 2219/10 (2013.01); B01D 53/77 (2013.01); B01D 53/96 (2013.01); B01D 2259/80 (2013.01);
Abstract

A catalytic reactor () is provided for purposes of effecting therewith the removal of nitrogen oxides from a process gas (F) that includes at least two catalyst bed segments (), each of which is provided with a closing device (). The catalytic reactor () is operative for causing said process gas (F) to flow through a first catalyst bed segment (). Said process gas (F) is at a first temperature at which the sulphur trioxide that is entrained in said hot process gas is at least partially precipitated out on to the catalytic material that said first catalyst bed segment () embodies. Periodically said closing device () is operated in order to thereby isolate said first bed segment () from the flow therethrough of said hot process gas (F). A regeneration system () is also provided that is operative for purposes of causing a regenerating gas to flow through the first bed segment (). In addition, a sulphur trioxide removal device () is provided, which is separate from said catalytic reactor (), and which is operative for purposes of effecting therewith the removal of the sulphur trioxide from said regenerating gas.


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