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24/06/2005 - Controller General of Patents, Designs, and Trade Marks

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(12) PATENT APPLICATION PUBLICATION<br />

(19) INDIA (21)<br />

(22) Date <strong>of</strong> filing <strong>of</strong> Application: <strong>06</strong>/<strong>06</strong>/2003 (43)<br />

Application No: 581/MUMNP/2003 A<br />

Publication Date: <strong>24</strong>/<strong>06</strong>/<strong>2005</strong><br />

(54) Title <strong>of</strong> the invention: METHOD FOR LEACHING COPPER CONCENTRATE<br />

(51) International Classification : C 22 B 15/00 (71)<br />

(31) Priority Document No. : 200002802<br />

(32) Priority Date : 20/12/2000<br />

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

(86)<br />

International Application<br />

No.<br />

: PCT/FI01/01080<br />

Filing Date : 11/12/2001<br />

(87) International Publication<br />

No.<br />

: WO 02/50319 A1<br />

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

Application No.<br />

: NIL<br />

Filed on : N.A.<br />

(62)<br />

(57) Abstract:<br />

Divisional to Application<br />

No.<br />

: NIL<br />

Filed on : N.A.<br />

(72)<br />

Name <strong>of</strong> the Applicant:<br />

OUTOKUMPU OYJ<br />

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

RIIHITONTUNTIE 7,<br />

FIN-02200 ESPOO, FINLAND.<br />

Name <strong>of</strong> the Inventors:<br />

1. HAMALAINEN MATTI<br />

Filed U/S 5(2) before the<br />

<strong>Patents</strong> (Amendment)<br />

Ordinance, 2004: NO<br />

This invention relates to a method where sulfidic iron-bearing copper concentrate is leached on the<br />

countercurrent principle, in a chloride environment. The leaching takes place with the aid <strong>of</strong> bivalent<br />

copper <strong>and</strong> an oxygen-bearing gas as a multistage continuous process, under normal pressure, at a<br />

temperature, which as highest corresponds to the boiling point <strong>of</strong> the solution. Part <strong>of</strong> the insoluble solid<br />

matter is returned, counter to the main flow <strong>of</strong> solid matter, to one <strong>of</strong> the previous leaching stages or<br />

reactors where, as a result <strong>of</strong> the extended leaching time, the leach waste iron is recovered mostly as<br />

hematite.<br />

(FIG.: NIL)<br />

Total Pages: 9.<br />

The Patent Office Journal <strong>24</strong>.<strong>06</strong>.<strong>2005</strong> 17785

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