-
公开(公告)号:DE59200105D1
公开(公告)日:1994-05-11
申请号:DE59200105
申请日:1992-02-26
Applicant: DEGUSSA
Inventor: DIEHL MANFRED DR , FISCHER JOACHIM , WOLF HUBERT
Abstract: The invention relates to a process for detoxifying aqueous solutions containing cyanohydrins, in particular glycolonitrile and/or nitriles, which additionally contain decomposition catalysts for peroxide compounds, in particular manganese compounds, by perhydrolysis of the cyano compounds at temperatures of 5 to 80 DEG C and pHs of 8 to 12, with one or more peroxide compounds selected from the group comprising the alkali metal percarbonates, alkali metal perborates and alkaline earth metal perborates and the alkaline earth metal peroxides, the peroxide compounds mentioned being added as such to the solution to be detoxified or are formed in situ in the solution to be detoxified. Sodium percarbonate is preferably used. … The process according to the invention is more effective and more economical than the previously known process using hydrogen peroxide.
-
公开(公告)号:AU645203B2
公开(公告)日:1994-01-06
申请号:AU1710592
申请日:1992-05-22
Applicant: DEGUSSA
Inventor: FISCHER JOACHIM , WOLF HUBERT , DIEHL MANFRED
Abstract: The invention relates to a process for the separation of hydrogen cyanide from gases and exhaust gases by through-flow or circulation scrubbing, formaldehyde being added in a controlled manner to the aqueous scrubbing liquid for glycol nitrile formation; the control is carried out via the measurement of the HCN tension in a branched-off measurement stream, which is first treated with hydrogen peroxide in such a manner that after 1 to 100 seconds free H2O2 is still detectable, and is set to a constant pH prior to the HCN tension measurement. The process avoids a formaldehyde overdose which could not always be avoided in previously known processes having a control of the formaldehyde addition via the measurement of the cyanide-specific redox potential.
-
公开(公告)号:MX169904B
公开(公告)日:1993-07-30
申请号:MX895987
申请日:1987-10-23
Applicant: DEGUSSA
Inventor: FISCHER JOACHIM , KNORRE HELMUT , GRIFFITHS ANDREW , LOROSCH JURGEN
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.
-
公开(公告)号:DE59000101D1
公开(公告)日:1992-05-27
申请号:DE59000101
申请日:1990-08-22
Applicant: DEGUSSA
Inventor: FISCHER JOACHIM , WOLF HUBERT
Abstract: The content of halo-organic pollutants in water is lowered to residual AOX values below 1 mg/l, preferably below 0.1 mg/l by adjusting the Fe2+ comtent of the water to 20 to 1000 mg/l, adding a precipitated or pyrogenic silicic acid, converting 20 to 1000 mg of the Fe2+ into Fe3+ by adding in an oxidation agent, preferably hydrogen peroxide, and separating the iron (III) hydroxy complexes formed and the silicic acid, which contain the halo-organic pollutants in an adsorbed state, at pH 5-10. The method can be controlled in a simple manner as regards the addition of Fe2+ and oxidation agent via the Fe2+/Fe3+ redox potential.
-
公开(公告)号:PH24130A
公开(公告)日:1990-03-05
申请号:PH36007
申请日:1987-10-30
Applicant: DEGUSSA
Inventor: KNORRE HELMUT DR , LOROSCH JURGEN 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.
-
公开(公告)号:FI75140C
公开(公告)日:1988-05-09
申请号:FI821694
申请日:1982-05-13
Applicant: DEGUSSA
Inventor: KNORRE HELMUT , FISCHER JOACHIM , STUETZEL KLAUS
-
公开(公告)号:PT86035A
公开(公告)日:1987-11-01
申请号:PT8603587
申请日:1987-10-29
Applicant: DEGUSSA
Inventor: KNORRE HELMUT , GRIFFITHS ANDREW , LOROESCH JUERGEN , FISCHER JOACHIM
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:DE3534677C1
公开(公告)日:1987-04-30
申请号:DE3534677
申请日:1985-09-28
Applicant: DEGUSSA
Inventor: FISCHER JOACHIM , KNORRE HELMUT DIPL-CHEM DR
IPC: B01D53/14 , B01D53/30 , B01D53/34 , B01D53/54 , B01D53/58 , C10K1/10 , G01N27/416 , A62D3/00 , G05D21/02
Abstract: In purifying gas wash waters containing cyanide with formaldehyde, the exact dosing of formaldehyde presents a problem, especially with strongly fluctuating cyanide contents. By continuous potentiometric measurement in a side stream which is regulated to a pH of 7 to 10, while the pH of the main stream remains unchanged, the formaldehyde can be adjusted safely to any cyanide content.
-
公开(公告)号:DE3262541D1
公开(公告)日:1985-04-18
申请号:DE3262541
申请日:1982-06-25
Applicant: DEGUSSA
Inventor: KNORRE HELMUT DR DIPL CHEM , FISCHER JOACHIM , STUTZEL KLAUS
Abstract: There is provided a continuous process for the lowering of the content of toxic materials in waste waters which also contain other oxidizable materials by quickly and continuously ascertaining the requirement of hydrogen peroxide, namely by potentiometric determination of the oxidizing agent requirement in a branched-off side-stream using a strong oxidizing agent, such as peroxymonosulfate, peroxydisulfate, permanganate, hypochlorite or ozone, which acts more quickly than hydrogen peroxide under comparable conditions.
-
公开(公告)号:IT7950971D0
公开(公告)日:1979-12-03
申请号:IT5097179
申请日:1979-12-03
Inventor: KNORRE HELMUT , FISCHER JOACHIM
Abstract: In the detoxification of waste waters containing nitrite ions by means of hydrogen peroxide the addition of hydrogen peroxide is automatically controllable by adding the hydrogen peroxide continuously or in portions with continuous measurement of the pH and stopping the addition when no further reduction of the pH is caused by it. By control of the hydrogen peroxide addition through the change of the pH it is guaranteed that sufficient hydrogen peroxide is added to reach a complete detoxification of the waste water while on the other hand there is not wasted hydrogen peroxide unnecessarily.
-
-
-
-
-
-
-
-
-