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:
Dec. 22, 1998

Filed:

Aug. 20, 1996
Applicant:
Inventors:

Karl T Chuang, Edmonton, CA;

Mingqian Zhang, Edmonton, CA;

Bing Zhou, Edmonton, CA;

Assignee:

Hydrocarbon Technologies, Inc., Lawrenceville, NJ (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01J / ; B01J / ; A62D / ;
U.S. Cl.
CPC ...
502314 ; 502304 ; 502316 ; 502318 ; 502320 ; 502327 ; 502331 ; 502333 ; 502334 ; 4232453 ; 4232451 ; 588205 ; 588206 ; 588207 ;
Abstract

A catalyst for effective oxidation of volatile organic compounds (VOCs) includes 0.010-2 wt. % of a noble metal such as platinum in combination with 0.5-15 wt. % of a transition metal oxide such as chromium oxide (Cr.sub.2 O.sub.3), with at least the noble metal being deposited as a thin outer layer or shell not exceeding 0.10 mm thickness on a porous inert support such as alumina or silica having surface area of 10-400 m.sup.2 /g. The catalyst is made by adding the transition metal oxide such as chromium oxide (Cr.sub.2 O.sub.3) to the support material particles, and then subsequently mixing a solution of ammonium platinum nitrate with a suitable carrier liquid so as to form a 'cluster' structure on the support material and which limits penetration of the active noble metal into the porous support, then drying, reducing, and calcining the metals-loaded support material. This catalyst composition and structure is highly effective for the oxidative destruction of VOCs in vapor form at concentrations of 1 ppm--5 vol. % and at reaction temperatures of 50.degree.-500.degree. C., 0-600 psig pressure, and space velocity of 1000-200,000 hr.sup.-1 to produce essentially only carbon dioxide and water products.


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