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

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(12) PATENT APPLICATION PUBLICATION<br />

(19) INDIA (21) APPLICATION No:<br />

1250/MAS/1998A<br />

(22) Date <strong>of</strong> filing <strong>of</strong> Application:09/06/1998 (43) Publication Date: 09/06/2006<br />

(54) Title <strong>of</strong> <strong>the</strong> invention:<br />

HYDROCONVERSION OF VACUUM<br />

DISTILLATES AND DEASPHALTED<br />

OIL IN FIXED BEDS AND BOILING<br />

BEDS<br />

(51) International classification: C10G<br />

065/00, C10G 069/04, C10G 001/08<br />

(31) Priority Document No.97/09.272<br />

(32) Priority Date: 10/06/1997<br />

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

(87) WIPO No.:<br />

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

Application No. :<br />

Filed on:<br />

(62) Divisional to<br />

Application No.:<br />

Filed on:<br />

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

INSTITUT FRANCAIS DU PETROLE<br />

Address <strong>of</strong> Applicant:<br />

4 AVENUE DE BOIS PREAU 92500,<br />

REUIL MALMAISON, FRANCE.,<br />

FRANCE.<br />

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

MOREL FREDERIC,<br />

DUPLAN JEEN-LUC,<br />

BILLON ALAIN,<br />

KRESSMANN STEPHANE<br />

(57) Abstract<br />

The present invention relates to a process for <strong>the</strong> conversion <strong>of</strong> a hydrocarbon fraction comprising a step a) for<br />

treating a hydrocarbon charge in <strong>the</strong> presence <strong>of</strong> a hydrogen in at least one reactor containing at least one<br />

hydrodesulphurisation catalyst in a fixed bed under conditions that make it possible to obtain a liquid effluent with a<br />

reduced sulphur content, a step) for treating at least a part - <strong>of</strong> <strong>the</strong> liquid effluent originating from step a) in <strong>the</strong><br />

presence <strong>of</strong> hydrogen in at least one three-phase reactor, containing at least one hydrotreatment catalyst in a boiling<br />

bed, operating with an ascending stream <strong>of</strong> liquid and gas, said reactor comprising at least one means <strong>of</strong> withdrawing<br />

<strong>the</strong> catalyst from said reactor situated near <strong>the</strong> bottom <strong>of</strong> <strong>the</strong> reactor and at least one means <strong>of</strong> making up fresh<br />

catalyst in said reactor situated near <strong>the</strong> top <strong>of</strong> said reactor, and a step c) in which at least part <strong>of</strong> <strong>the</strong> product obtained<br />

in step b) is passed to a distillation zone from which are recovered a gas fraction, a motor fuel fraction <strong>of</strong> <strong>the</strong> petrol<br />

type, a motor fuel fraction <strong>of</strong> <strong>the</strong> diesel type, and a liquid fraction which is heavier than <strong>the</strong> diesel type fraction. This<br />

process may also contain a step d) for <strong>the</strong> catalyst cracking <strong>of</strong> <strong>the</strong> heavy fraction obtained in step c).<br />

The Patent Office Journal 09/06/2006 10782

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