Process for the aromatization of a methane-containing gas stream using zirconium hydrogen acceptor particles
US-2016368836-A1 · Dec 22, 2016 · US
US9399213B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9399213-B2 |
| Application number | US-201514793974-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 8, 2015 |
| Priority date | Mar 29, 2011 |
| Publication date | Jul 26, 2016 |
| Grant date | Jul 26, 2016 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided is a practical method for dry-separating arsenic compounds from a used NOx removal catalyst contaminated with arsenic. The method for removing arsenic compounds comprises heat-treating a NOx removal catalyst contaminated with arsenic compounds at a predetermined temperature in a reducing atmosphere while exposing the catalyst to hydrocarbon compounds (except CH 4 ) or oxygen-containing carbon compound.
Opening claim text (preview).
The invention claimed is: 1. An apparatus for removing an arsenic compound, comprising a treatment unit which conducts heat-treatment of a NOx removal catalyst contaminated with the arsenic compound at a predetermined temperature in a reducing atmosphere while exposing the catalyst to hydrocarbon compounds except CH 4 or oxygen-containing carbon compounds. 2. The apparatus for removing an arsenic compound according to claim 1 , wherein the hydrocarbon compounds and the oxygen-containing carbon compounds are gaseous at the predetermined temperature. 3. The apparatus for removing an arsenic compound according to claim 1 , wherein the predetermined temperature is in a range of greater than 300° C. to 600° C. 4. The apparatus for removing an arsenic compound according to claim 1 , wherein the treatment unit exposes the NOx removal catalyst contaminated with the arsenic compound in a product form as is or after made into a particle form by grinding treatment to the hydrocarbon compounds or the oxygen-containing carbon compounds. 5. An apparatus for regenerating the NOx removal catalyst by removing the arsenic compound comprising the apparatus according to claim 1 . 6. The apparatus for regenerating a NOx removal catalyst according to claim 5 comprising a heat treatment unit which conducts heat-treatment of the NOx removal catalyst from which the arsenic compound has been removed at 250° C. or more in an oxygen atmosphere.
Controlling the temperature · CPC title
Treating with free oxygen-containing gas · CPC title
of catalysts comprising metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 · CPC title
Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title
Stationary reactors without moving elements inside · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.