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公开(公告)号:AU2003280430A1
公开(公告)日:2004-01-19
申请号:AU2003280430
申请日:2003-06-25
Applicant: CORNING INC
Inventor: BOGER THORSTEN R , SORENSEN CHARLES M JR , ROY SHANTANU
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公开(公告)号:AU2002340319A1
公开(公告)日:2003-06-23
申请号:AU2002340319
申请日:2002-10-28
Applicant: CORNING INC
Inventor: BOGER THORSTEN R , SORENSEN CHARLES M JR
Abstract: Systems, processes, and reactors for the catalytic reforming of naphtha are provided. Embodiments of the invention include reactors comprising monolithic catalyst having honeycomb-type structure that allows for improved efficiency, productivity, and reaction selectivity over conventional catalytic reforming technology.
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公开(公告)号:EP1516036A4
公开(公告)日:2006-11-29
申请号:EP03742305
申请日:2003-06-25
Applicant: CORNING INC
Inventor: BOGER THORSTEN R , SORENSEN CHARLES M JR , ROY SHANTANU
IPC: B01J19/24 , B01J23/38 , B01J23/70 , B01J23/755 , B01J35/04 , C10G45/04 , C10G45/32 , C10G45/34 , C10G45/46 , C10G49/00 , C10G65/04 , C10G65/06 , C10G65/08 , C10G69/06 , C10G45/00 , B01J10/00 , C07C7/163 , C07C7/167
CPC classification number: C10G65/08 , B01J19/2485 , B01J23/38 , B01J23/70 , B01J23/755 , B01J35/04 , B01J2219/00006 , B01J2219/00087 , B01J2219/0011 , C10G45/46 , C10G65/04 , C10G65/06 , C10G2400/02
Abstract: Systems and processes for the hydrotreatment of pyrolysis gasoline comprising reactors, monolithic catalyst beds and hydrogen-containing treatment gases that allow for improved efficiency and productivity over conventional trickle bed processes and systems for such hydrotreatment .
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公开(公告)号:EP1355732A4
公开(公告)日:2006-02-08
申请号:EP01995265
申请日:2001-11-29
Applicant: CORNING INC
Inventor: BOGER THORSTEN R
CPC classification number: B01J19/2485 , B01J19/1875 , B01J19/1881 , B01J19/246 , B01J19/2465 , B01J2219/00094 , B01J2219/00768 , B01J2219/00779
Abstract: An improved recirculating tank reactor (10) incorporating the advantages of a fixed catalyst includes a monolithic honeycomb catalyst (12) positioned within the tank in such a manner so as to provide an adjacent bypass passageway (20). Internal flow activation means (24) are provided for recirculating the reactant liquid (a) within the tank in such a manner that it sequentially flows through channels (18) in the catalyzed honeycomb substrate (12) and around the substrate through the bypass passageway (20).
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