SI
SI
discoversearch

We've detected that you're using an ad content blocking browser plug-in or feature. Ads provide a critical source of revenue to the continued operation of Silicon Investor.  We ask that you disable ad blocking while on Silicon Investor in the best interests of our community.  If you are not using an ad blocker but are still receiving this message, make sure your browser's tracking protection is set to the 'standard' level.
Gold/Mining/Energy : Plastic2Oil, Inc.
PTOI 0.00010000.0%Oct 22 11:09 AM EST

 Public ReplyPrvt ReplyMark as Last ReadFilePrevious 10Next 10PreviousNext  
To: donpat who wrote (57)3/8/2010 11:01:58 AM
From: scion of 621
 
Primary Class: 585/241

freepatentsonline.com

One example:

Method for catalytically cracking waste plastics and apparatus for catalytically cracking waste plastics

United States Patent Application 20070173673

Kind Code: A1

To provide a method for catalytically cracking waste plastics wherein the efficiency in decomposition is high; even polyethylene composed of linear chain molecules difficult in decomposition is decomposable at a low temperature and decomposed residue is hardly produced; the process is simple since dechlorination can be achieved at the same time with catalytically cracking waste plastics in one reaction vessel; and oil fractions can be recovered at 50% or more on a net yield basis. The method for catalytically cracking waste plastics of the present invention has a constitution in which waste plastics are loaded as a raw material into a granular FCC catalyst heated to a temperature range from 350° C. to 500° C. inside a reaction vessel, thereby decomposing and gasifying the waste plastics in contact with the FCC catalyst.

Inventors:
Fujimoto, Kaoru (Fukuoka, JP)
Li, Xiaohong (Fukuoka, JP)
Application Number: 11/588378
Publication Date: 07/26/2007
Filing Date: 10/27/2006

Assignee: Kitakyushu Foundation for the advancement of Industry, Science and Technology
Primary Class:585/241
Other Classes:422/198, 422/224
International Classes:C10G1/10; B01J8/10

View Patent Images:
Download PDF 20070173673
freepatentsonline.com

Related US Applications:20030153797 Process for producing a liquid fuel composition August, 2003 Percell
20030009067 Anoxic reaction apparatus and process for obtaining an anoxic reaction therein January, 2003 Bouziane et al.
20030109761 Method and equipment for pre-treatment of used tyres before a pyrolysis process June, 2003 Suominen
20090062581 METHODS AND APPARATUS FOR CONVERTING WASTE MATERIALS INTO FUELS AND OTHER USEFUL PRODUCTS March, 2009 Appel et al.
20070135667 Method of reutilization and method of shaping of waste plastic June, 2007 Araki et al.
20020119089 Process for pyrolyzing tire shreds and tire pyrolysis systems August, 2002 Masemore et al.

The FCC catalyst used is a solid acid catalyst based on synthetic zeolite which is granulated into granular particles of 40 to 80 µm used in the FCC (fluid catalyst cracking) process of petroleum. Since the FCC catalyst is substantially similar to waste plastics in mean specific gravity of 0.74 to 0.91, it can be mixed well with waste plastics inside a reaction vessel. Off-specification catalysts discharged from catalyst manufacturers and waste catalysts discharged from petroleum refinery plants may also be used. A mixture of these catalysts may also be used.

The waste catalyst is called FCC (U) (fluid catalyst cracking (used)) and obtained by regenerating catalysts used in fluid catalytic cracking for selectively catalytically cracking a wide variety of petroleum fractions covering light oil to normal pressure residue. It is also called an equivalent catalyst or regenerated catalyst. In petroleum refining plants, the catalyst is recycled between a catalytic cracking area and a regeneration area. A new catalyst is constantly supplied in a predetermined quantity to offset catalytic deterioration.

freepatentsonline.com
Report TOU ViolationShare This Post
 Public ReplyPrvt ReplyMark as Last ReadFilePrevious 10Next 10PreviousNext