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official journal of the patent office - Controller General of Patents ...

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(12)<br />

(19)<br />

(22)<br />

PATENT APPLICATION PUBLICATION<br />

INDIA<br />

Date <strong>of</strong> filing <strong>of</strong> Application: 21/06/2001<br />

(54) Title <strong>of</strong> <strong>the</strong> Invention: “Simultaneous Hydroprocessing <strong>of</strong> two Feed stocks”<br />

(51) International Classification : C07C 5/02<br />

(31) Priority Document No. : NIL<br />

(32) Priority Date : NIL<br />

(33) Name <strong>of</strong> priority country : USA<br />

(86) International application No. : NA<br />

Filing Date : NA<br />

(87) International Publication No. : NA<br />

(61) Patent <strong>of</strong> Addition to<br />

Application No.<br />

:<br />

N.A.<br />

(62) Divisional to Application No. : NIL<br />

Filed On : N.A.<br />

Total No. <strong>of</strong> pages : 22+01=23<br />

(21)<br />

(43)<br />

Application No.: 694/DEL/2001<br />

Publication Date:09/06/2006<br />

(71) Name <strong>of</strong> Applicant :<br />

UOP LLC,<br />

Address <strong>of</strong> <strong>the</strong> Applicant: USA, 25 East<br />

Algonquin Road, Des Plaines, Illinois 60017-<br />

5017, USA.<br />

(72) Name <strong>of</strong> <strong>the</strong> Inventor:<br />

TOM NELSON KALNES<br />

(57) Abstract: A catalytic hydrocracking process wherein a first hydrocarbonaceous feedstock is contacted with<br />

hydrogen and a metal promoted hydrocracking catalyst in a hydrocracking reaction zone at elevated temperature and<br />

pressure to obtain conversion to lower boiling hydrocarbons. The resulting hot, uncooled effluent from <strong>the</strong><br />

hydrocracking reaction zone is hot hydrogen stripped in a stripping zone maintained at essentially <strong>the</strong> same pressure<br />

as <strong>the</strong> hydrocracking zone to produce a first gaseous hydrocarbonaceous stream and a first liquid hydrocarbonaceous<br />

stream is preferably recycled to <strong>the</strong> hydrocaracking reaction zone. A second hydrocarbonaceous feedstock having a<br />

boiling temperature range lower than that <strong>of</strong> <strong>the</strong> first hydrocarbonaceous feedstock is introduced into an upper end <strong>of</strong><br />

<strong>the</strong> stripper to serve as reflux. The first gaseous hydrocarbonaceous stream is removed from <strong>the</strong> stripper and passed to<br />

a post-treat hydrogenation reaction zone to saturate aromatic compounds.<br />

The Patent Office Journal 09/06/2006 11095<br />

A

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