ITBO940512A1 - PROCESS OF ACCELERATED CORROSION AND SEPARATION OF METALS IN METAL ATTACKING PLANTS BY AMMONIA TREATMENT - Google Patents
PROCESS OF ACCELERATED CORROSION AND SEPARATION OF METALS IN METAL ATTACKING PLANTS BY AMMONIA TREATMENT Download PDFInfo
- Publication number
- ITBO940512A1 ITBO940512A1 IT94BO000512A ITBO940512A ITBO940512A1 IT BO940512 A1 ITBO940512 A1 IT BO940512A1 IT 94BO000512 A IT94BO000512 A IT 94BO000512A IT BO940512 A ITBO940512 A IT BO940512A IT BO940512 A1 ITBO940512 A1 IT BO940512A1
- Authority
- IT
- Italy
- Prior art keywords
- process according
- corrosive
- nitrate
- electrolytic cell
- copper
- Prior art date
Links
- 238000005260 corrosion Methods 0.000 title claims abstract description 8
- 230000007797 corrosion Effects 0.000 title claims abstract description 8
- 238000000034 method Methods 0.000 title claims description 18
- 230000008569 process Effects 0.000 title claims description 18
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims description 10
- 229910052751 metal Inorganic materials 0.000 title claims description 10
- 239000002184 metal Substances 0.000 title claims description 10
- 229910021529 ammonia Inorganic materials 0.000 title claims description 5
- 238000000926 separation method Methods 0.000 title description 6
- 150000002739 metals Chemical class 0.000 title description 3
- 229910002651 NO3 Inorganic materials 0.000 claims abstract description 16
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 11
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 6
- 230000008929 regeneration Effects 0.000 claims description 3
- 238000011069 regeneration method Methods 0.000 claims description 3
- 229910052720 vanadium Inorganic materials 0.000 claims description 3
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 claims description 2
- 229910017052 cobalt Inorganic materials 0.000 claims description 2
- 239000010941 cobalt Substances 0.000 claims description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 2
- 229910052711 selenium Inorganic materials 0.000 claims description 2
- 239000011669 selenium Substances 0.000 claims description 2
- 238000005868 electrolysis reaction Methods 0.000 claims 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 13
- 229910052802 copper Inorganic materials 0.000 abstract description 13
- 239000010949 copper Substances 0.000 abstract description 13
- 230000001133 acceleration Effects 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 4
- 230000009466 transformation Effects 0.000 abstract description 3
- 230000009471 action Effects 0.000 abstract description 2
- 230000001737 promoting effect Effects 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 2
- 239000013539 acceleration additive Substances 0.000 description 1
- -1 ammonium ions Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000003442 weekly effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F1/00—Etching metallic material by chemical means
- C23F1/46—Regeneration of etching compositions
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
- ing And Chemical Polishing (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Le versioni correnti considerano il nitrato contenuto nella cella elettrolitica un fattore di disturbo e cercano di eliminarlo in tutto o in massima parte dalla soluzione corrosiva. La presente invenzione propone di far funzionare gli impianti per il trattamento di corrosione con un determinato contenuto ottimale di nitrato, che provoca una considerevole accelerazione della velocità dell'azione corrosiva e propone di limitarne la concentrazione aggiungendo riducenti, i quali per esempio nel rame, presentano l'ulteriore vantaggio di favorire nella cella elettrolitica la trasformazione accelerata del rame II in rame I.The current versions consider the nitrate contained in the electrolytic cell to be a disturbing factor and try to eliminate it in whole or in large part from the corrosive solution. The present invention proposes to operate the plants for the treatment of corrosion with a certain optimal content of nitrate, which causes a considerable acceleration of the speed of the corrosive action and proposes to limit its concentration by adding reducing agents, which for example in copper present the further advantage of promoting the accelerated transformation of copper II into copper I in the electrolytic cell.
Description
DESCRIZIONE DESCRIPTION
dell'invenzione industriale dal titolo "PROCESSO DI CORROSIONE ACCELERATA E DI SEPARAZIONE DEI METALLI IN IMPIANTI DI ATTACCO DEI METALLI MEDIANTE TRATTAMENTO AMMONIACALE" of the industrial invention entitled "PROCESS OF ACCELERATED CORROSION AND SEPARATION OF METALS IN METAL ATTACKING PLANTS BY MEANS OF AMMONIA TREATMENT"
RIASSUNTO SUMMARY
Le versioni correnti considerano il nitrato contenuto nella cella elettrolitica un fattore di disturbo e cercano di eliminarlo in tutto o in massima parte dalla soluzione corrosiva . Current versions consider the nitrate contained in the electrolytic cell as a disturbing factor and try to eliminate it in whole or in part from the corrosive solution.
L'invenzione propone di far funzionare gli impianti di attacco dei metalli con un determinato contenuto ottimale di nitrato, che provoca una considerevole accelerazione della velocità dell'azione corrosiva, e propone di limitarne la concentrazione aggiungendo riducenti, i quali, per esempio nel rame, presentano l'ulteriore vantaggio di favorire nella cella elettrolitica la trasformazione accelerata del rame II in rame I. The invention proposes to operate the metal etching systems with a given optimal content of nitrate, which causes a considerable acceleration of the rate of the corrosive action, and proposes to limit its concentration by adding reducing agents, which, for example in copper, have the further advantage of favoring the accelerated transformation of copper II into copper I in the electrolytic cell.
DESCRIZIONE DETTAGLIATA DETAILED DESCRIPTION
Gli impianti di attacco dei metalli, che lavorano con prodotti corrosivi ammoniacali, sono particolarmente adatti alla rigenerazione del prodotto corrosivo in processi di riciclaggio, in cui il metallo corroso viene contemporaneamente separarato metallicamente in celle elettrolitiche . Metal attack systems, which work with ammonia corrosive products, are particularly suitable for the regeneration of the corrosive product in recycling processes, in which the corroded metal is simultaneously metallically separated in electrolytic cells.
Per rendere economici tali impianti di riciclaggio, è molto importante che la velocità di corrosione, nonché quella di separazione del metallo nella cella elettrolitica, venga accelerata. To make these recycling plants economical, it is very important that the corrosion rate, as well as the separation rate of the metal in the electrolytic cell, is accelerated.
A questo proposito, è importante che per quanto possibile, nel corso del processo di corrosione e di rigenerazione e nel processo di separazione del metallo, i materiali risultanti non siano presenti in concentrazione eccessiva. Per quanto possibile, sono da evitare reazioni secondarie di disturbo. Scopo dell'invenzione è quello di indicare un processo che si avvicini il più possibile a questa meta ideale. In this regard, it is important that as far as possible, in the course of the corrosion and regeneration process and in the metal separation process, the resulting materials are not present in excessive concentration. As far as possible, secondary disturbing reactions should be avoided. The purpose of the invention is to indicate a process that comes as close as possible to this ideal goal.
A questo proposito, è da attribuire al concetto dell'invenzione una particolare importanza, dato che negli attuali impianti con cella elettrolitica, l'effetto secondario di disturbo - e precisamente la formazione di ossigeno e l'ossidazione degli ioni di ammonio in nitrato come reazione secondaria - è decisamente utile. In this regard, particular importance is to be attributed to the concept of the invention, since in current systems with electrolytic cell, the secondary disturbance effect - namely the formation of oxygen and the oxidation of ammonium ions into nitrate as a reaction secondary - is definitely useful.
Per esempio, il brevetto pubblicato DE 4218 843 Al descrive un processo, che propone la sottrazione del nitrato dal prodotto corrosivo mediante reazione con un riducente. For example, the published patent DE 4218 843 A1 describes a process, which proposes the removal of the nitrate from the corrosive product by reaction with a reducing agent.
In questo caso, l'effetto di accelerazione del nitrato sul processo corrosivo è stato totalmente trascurato, effetto che, in caso di sottrazione dal prodotto corrosivo, non si verifica più se il contenuto residuo è compreso fra 10 e 40 g/l. In this case, the acceleration effect of the nitrate on the corrosive process has been totally neglected, an effect which, in case of subtraction from the corrosive product, no longer occurs if the residual content is between 10 and 40 g / l.
Secondo l'invenzione, il nitrato che si forma nel prodotto corrosivo sugli elettrodi della cella elettrolitica ha una concentrazione compresa fra un minimo di 50 e 200 g/1. In questo modo, si ottiene una notevole accelerazione del processo corrosivo. According to the invention, the nitrate which forms in the corrosive product on the electrodes of the electrolytic cell has a concentration comprised between a minimum of 50 and 200 g / l. In this way, a considerable acceleration of the corrosive process is obtained.
Per evitare l'eccessiva concentrazione di nitrato, si consiglia di aggiungere riducenti, se i valori dovessero aumentare troppo. To avoid excessive nitrate concentration, it is recommended to add reducing agents if the values increase too much.
Si consiglia la formaldeide come riducente particolarmente efficace, prodotto sperimentato, noto in ambito galvanotecnico. Formaldehyde is recommended as a particularly effective reducing agent, an experimented product, known in the electroplating field.
Un maggior contenuto di nitrato, associato a riducenti aggiunti come indicato dall'invenzione, migliora anche la separazione dei metalli nella cella elettrolitica, dato che, per esempio per il rame, viene accelerata la riduzione da rame II a rame I, necessaria per la separazione del rame stesso. A higher nitrate content, associated with added reducing agents as indicated by the invention, also improves the separation of metals in the electrolytic cell, since, for example for copper, the reduction from copper II to copper I, necessary for the separation, is accelerated. of copper itself.
Il processo proposto dall'invenzione ad alto contenuto di nitrato ha l'ulteriore vantaggio di essere utilizzabile anche per determinati additivi di accelerazione, per esempio a base di composti contenenti vanadio. The process proposed by the invention with a high nitrate content has the further advantage of being usable also for certain acceleration additives, for example based on compounds containing vanadium.
L'invenzione propone anche l'aggiunta di acceleratori contenenti selenio o cobalto. The invention also proposes the addition of accelerators containing selenium or cobalt.
Sono evidenti i vantaggi dei processi proposti, dato che in essi non si formano sostanze che incidano sul processo di corrosione. The advantages of the proposed processes are evident, since they do not form substances that affect the corrosion process.
Si elencano esempi di soluzione corrosiva, come da invenzione, con tracce di vanadio come acceleratore: Examples of corrosive solutions are listed, as per invention, with traces of vanadium as an accelerator:
Le soluzioni 1 e 2 contengono inoltre ammoniaca per la regolazione del valore del pH alcalino. Solutions 1 and 2 also contain ammonia for adjusting the alkaline pH value.
E' noto che la velocità di corrosione dipende dalla temperatura e dal valore pH. Negli esempi di soluzione corrosiva proposti dall'invenzione sono risultati ottimali temperature comprese fra 35°C e 60°C, valori pH compresi fra 8,1 e 8,8 e un contenuto di nitrato di 70-80 g/1. It is known that the corrosion rate depends on the temperature and the pH value. In the examples of corrosive solution proposed by the invention, temperatures ranging from 35 ° C to 60 ° C, pH values ranging from 8.1 to 8.8 and a nitrate content of 70-80 g / 1 were found to be optimal.
Non è cruciale aggiungere e dosare i riducenti per evitare concentrazioni di nitrati troppo elevate. Nella maggior parte dei casi, è sufficiente una analisi e una aggiunta settimanali . It is not crucial to add and dose the reducing agents to avoid too high nitrate concentrations. In most cases, a weekly analysis and addition is sufficient.
Ovviamente è anche possibile dosare l'aggiunta in maniera continua, per esempio mediante pompe dosatrici, dato che la formazione di nitrato è più o meno proporzionale alla quantità di rame separata e/o al bilancio di corrente della cella elettrolitica e come tale, può essere facilmente calcolata a priori. Obviously it is also possible to dose the addition continuously, for example by means of dosing pumps, since the formation of nitrate is more or less proportional to the quantity of separated copper and / or to the current balance of the electrolytic cell and as such, it can be easily calculated in advance.
Se l'aggiunta dei riducenti viene dosata in maniera continua, si consiglia di effettuarla vicino alla cella elettrolitica, per esempio all'alimentazione, in modo da ottenere un risultato migliore, come ad esempio nella trasformazione del rame II in rame I. If the addition of reducing agents is dosed continuously, it is recommended to carry out it close to the electrolytic cell, for example at the power supply, in order to obtain a better result, such as for example in the transformation of copper II into copper I.
Claims (7)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4339320A DE4339320A1 (en) | 1993-11-18 | 1993-11-18 | Process for accelerated etching and deposition of metals in ammoniacal etching systems |
Publications (3)
Publication Number | Publication Date |
---|---|
ITBO940512A0 ITBO940512A0 (en) | 1994-11-17 |
ITBO940512A1 true ITBO940512A1 (en) | 1996-05-17 |
IT1276359B1 IT1276359B1 (en) | 1997-10-30 |
Family
ID=6502857
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
IT94BO000512A IT1276359B1 (en) | 1993-11-18 | 1994-11-17 | ACCELERATED CORROSION PROCESS AND METAL SEPARATION IN METAL ATTACKING PLANTS USING AMMONIA TREATMENT |
Country Status (7)
Country | Link |
---|---|
JP (1) | JPH07197300A (en) |
CN (1) | CN1107902A (en) |
DE (1) | DE4339320A1 (en) |
FR (1) | FR2712607B1 (en) |
GB (1) | GB2283983B (en) |
HK (1) | HK1001095A1 (en) |
IT (1) | IT1276359B1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110042425A (en) * | 2019-04-23 | 2019-07-23 | 博罗县华盈科技有限公司 | A kind of heavy process for copper of alkaline etching waste liquid for producing direct electrowinning |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1294804A (en) * | 1970-07-24 | 1972-11-01 | Shipley Co | Etchant for cupreous metals |
BE789944A (en) * | 1971-10-12 | 1973-02-01 | Shipley Co | REGENERATION OF A USED COPPER ATTACK SOLUTION |
DE2216269A1 (en) * | 1972-04-05 | 1973-10-18 | Hoellmueller Maschbau H | METHOD OF ETCHING COPPER AND COPPER ALLOYS |
DE3305319A1 (en) * | 1983-02-16 | 1984-08-16 | Siemens AG, 1000 Berlin und 8000 München | Electrolytic full regeneration process for an ammoniacal etching solution |
CA2029444A1 (en) * | 1990-03-21 | 1991-09-22 | Raymond A. Letize | System and process for etching with and regenerating, alkaline ammoniacal etchant solution |
AT395177B (en) * | 1990-07-05 | 1992-10-12 | Provera Gmbh | RESOLUTION |
WO1993009267A1 (en) * | 1991-11-09 | 1993-05-13 | Hans Höllmüller Maschinenbau GmbH & Co. | Process for regenerating an ammoniacal etching agent and device for implementing it |
DE4218843C2 (en) * | 1991-11-09 | 1994-04-28 | Hoellmueller Maschbau H | Process for the regeneration of an ammoniacal etchant and device for carrying out this process |
-
1993
- 1993-11-18 DE DE4339320A patent/DE4339320A1/en not_active Ceased
-
1994
- 1994-11-10 GB GB9422669A patent/GB2283983B/en not_active Expired - Fee Related
- 1994-11-17 CN CN94120116.3A patent/CN1107902A/en active Pending
- 1994-11-17 JP JP6283829A patent/JPH07197300A/en active Pending
- 1994-11-17 IT IT94BO000512A patent/IT1276359B1/en active IP Right Grant
- 1994-11-17 FR FR9413991A patent/FR2712607B1/en not_active Expired - Fee Related
-
1997
- 1997-12-31 HK HK97102708A patent/HK1001095A1/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
IT1276359B1 (en) | 1997-10-30 |
GB9422669D0 (en) | 1995-01-04 |
ITBO940512A0 (en) | 1994-11-17 |
CN1107902A (en) | 1995-09-06 |
FR2712607B1 (en) | 1997-06-20 |
HK1001095A1 (en) | 1998-05-22 |
JPH07197300A (en) | 1995-08-01 |
GB2283983B (en) | 1997-07-02 |
GB2283983A (en) | 1995-05-24 |
DE4339320A1 (en) | 1995-05-24 |
FR2712607A1 (en) | 1995-05-24 |
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