-
公开(公告)号:AT73116T
公开(公告)日:1992-03-15
申请号:AT89113421
申请日:1989-07-21
Applicant: DEGUSSA
Inventor: GRIFFITHS ANDREW DR , AHSAN QUAMRUL M DR , NORCROSS ROY , KNORRE HELMUT DR , MERZ FRIEDRICH WILHELM
-
公开(公告)号:DE68900135D1
公开(公告)日:1991-08-08
申请号:DE68900135
申请日:1989-07-21
Applicant: DEGUSSA
Inventor: GRIFFITHS ANDREW DR , NORCROSS ROY , SCHERER GERHARD , MERZ FRIEDRICH WILHELM , GOS STEPHEN
-
公开(公告)号:AT64919T
公开(公告)日:1991-07-15
申请号:AT89113422
申请日:1989-07-21
Applicant: DEGUSSA
Inventor: GRIFFITHS ANDREW DR , NORCROSS ROY , SCHERER GERHARD , MERZ FRIEDRICH WILHELM , GOS STEPHEN
-
公开(公告)号:GR3002920T3
公开(公告)日:1993-01-25
申请号:GR910401465
申请日:1991-10-17
Applicant: DEGUSSA
Inventor: GRIFFITHS ANDREW DR , NORCROSS ROY
Abstract: The invention relates to processes for the detoxification of effluents from ore processing operations utilizing hydrogen peroxide. It has been found that the demand of hydrogen peroxide can be reduced considerably when a significant portion of magnetic substances contained in the effluent are being magnetially separated before treating the effluent utilizing hydrogen peroxide. The process of the invention can preferably be applied in the detoxification of tailings pulps which contain magnetic substances and cynnides.
-
公开(公告)号:DE68900333D1
公开(公告)日:1991-11-21
申请号:DE68900333
申请日:1989-03-14
Applicant: DEGUSSA
Inventor: GRIFFITHS ANDREW DR , NORCROSS ROY
Abstract: The invention relates to processes for the detoxification of effluents from ore processing operations utilizing hydrogen peroxide. It has been found that the demand of hydrogen peroxide can be reduced considerably when a significant portion of magnetic substances contained in the effluent are being magnetially separated before treating the effluent utilizing hydrogen peroxide. The process of the invention can preferably be applied in the detoxification of tailings pulps which contain magnetic substances and cynnides.
-
公开(公告)号:GR3002252T3
公开(公告)日:1992-12-30
申请号:GR910400847
申请日:1991-07-04
Applicant: DEGUSSA
Inventor: GRIFFITHS ANDREW DR , NORCROSS ROY , SCHERER GERHARD , MERZ FRIEDRICH WILHELM , GOS STEPHEN
-
公开(公告)号:DE68900917D1
公开(公告)日:1992-04-09
申请号:DE68900917
申请日:1989-07-21
Applicant: DEGUSSA
Inventor: GRIFFITHS ANDREW DR , AHSAN QUAMRUL M DR , NORCROSS ROY , KNORRE HELMUT DR , MERZ FRIEDRICH WILHELM
-
公开(公告)号:AU589818B2
公开(公告)日:1989-10-19
申请号:AU8053387
申请日:1987-10-30
Applicant: DEGUSSA
Inventor: LOROSCH JURGEN DR , FISCHER JOACHIM , GRIFFITHS ANDREW DR , KNORRE HELMUT DR
Abstract: Leaching of gold and/or silver from ores or ore concentrates in an aqueous alkaline cyanide solution with added hydrogen peroxide has so far not been used industrially, because it is uneconomical, i.e. the consumption of H2O2 and NaCN was unduly high. It has been found that the process can be made very economical and disadvantages of the conventional leaching technology can be avoided if the addition of the aqueous H2O2 solution is controlled via the concentration of the oxygen dissolved in the leaching solution, which contains 2 to 20 mg of O2 and preferably 7 to 13 mg of O2 per litre. Preferably, 0.5 to 5% by weight of H2O2 solutions are added under control. The process is applicable to agitation leaching and heap leaching, the H2O2 addition being controlled via measuring the O2 concentration in a measuring stream. At low consumption of H2O2 and NaCN, sometimes the gold yield is even increased and the leaching time is shortened.
-
公开(公告)号:DE3637082C1
公开(公告)日:1988-05-19
申请号:DE3637082
申请日:1986-10-31
Applicant: DEGUSSA
Inventor: KNORRE HELMUT DR , GRIFFITHS ANDREW DR , LOROESCH JUERGEN DR , FISCHER JOACHIM
IPC: C22B11/08
Abstract: Leaching of gold and/or silver from ores or ore concentrates in an aqueous alkaline cyanide solution with added hydrogen peroxide has so far not been used industrially, because it is uneconomical, i.e. the consumption of H2O2 and NaCN was unduly high. It has been found that the process can be made very economical and disadvantages of the conventional leaching technology can be avoided if the addition of the aqueous H2O2 solution is controlled via the concentration of the oxygen dissolved in the leaching solution, which contains 2 to 20 mg of O2 and preferably 7 to 13 mg of O2 per litre. Preferably, 0.5 to 5% by weight of H2O2 solutions are added under control. The process is applicable to agitation leaching and heap leaching, the H2O2 addition being controlled via measuring the O2 concentration in a measuring stream. At low consumption of H2O2 and NaCN, sometimes the gold yield is even increased and the leaching time is shortened.
-
-
-
-
-
-
-
-