EP0224790A1 - Verfahren zur Reinigung von Kathoden bei der Alkalichloridelektrolyse - Google Patents
Verfahren zur Reinigung von Kathoden bei der Alkalichloridelektrolyse Download PDFInfo
- Publication number
- EP0224790A1 EP0224790A1 EP19860115954 EP86115954A EP0224790A1 EP 0224790 A1 EP0224790 A1 EP 0224790A1 EP 19860115954 EP19860115954 EP 19860115954 EP 86115954 A EP86115954 A EP 86115954A EP 0224790 A1 EP0224790 A1 EP 0224790A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cell
- electrolysis
- catholyte
- cathodes
- alkalichlorides
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
Definitions
- the present invention relates to a method for removing cathodically deposited metallic contaminants in alkali metal chloride electrolysis.
- any conductive material that is stable under the electrolysis conditions can be used as the cathode material in alkali metal chloride electrolysis. Since the cell voltage is determined, among other things, by the deposition potential of the protons on the cathode, efforts are made to select a material with the lowest possible H2 overvoltage. Such materials are described in EP-A 129231, EP-A 129374 and DE-A 3322169.
- the low rate of corrosion of a material considered to be stable is sufficient to poison the catholyte with traces.
- the gettering effect of the cathode shifts the initially low H2 deposition potential to higher values, i.e. the cell voltage increases over time. This increase in voltage is directed among other things on the type and concentration of impurities; so z.
- B. a content of 1 ppm Fe in the supplied electrolyte can increase the cell voltage in the course of a few weeks to the level of a pure mild steel cathode.
- the object of the present invention is to eliminate these disadvantages which arise for optimal operation of an alkali metal chloride electrolysis.
- the present invention thus relates to a process for removing cathodically deposited metallic impurities in alkali metal chloride electrolysis, characterized in that the electrolytic cell is short-circuited and the electrolyte is discharged.
- the method according to the invention can be used regardless of the type of electrolysis, i.e. for the case that the electrolysis cell is an undivided cell, in particular an amalgam cell, or also for the case that the electrolysis cell is a divided cell, in particular a diaphragm or membrane cell.
- the short circuit should be carried out for 10 minutes to 10 hours. Particularly favorable results, also with regard to economic factors, are obtained if the short circuit is carried out for 30 minutes to 5 hours.
- An advantage of the method according to the invention is that existing installations can be used.
- a switch for bridging a cell is available according to the state of the art in order to be able to remove the corresponding cell from the circuit when repairing a cell or when replacing the diaphragm or the membranes.
- the method according to the invention avoids the use of non-electrolyte additives, such as those e.g. in EP-A 132 816 and EP-A 136 794.
- the contaminants deposited on the cathode dissolve again when the cell is electrically bridged.
- the advantages of the method according to the invention are also achieved in the case of the membrane or diphragm method. if only the catholyte is removed.
- the cathode chamber should also be flushed with catholyte.
- the running catholyte is not returned to the circuit, but is collected separately.
- the liquor obtained here can be used advantageously for alkalizing the brine before cleaning.
- the cell was rinsed with 1/3 of the amount of electrolyte usual during operation.
- the running catholyte had a 10-fold higher iron concentration than the feed.
- the catholyte thus enriched with detached Fe was collected separately and used for alkaline "brine precipitation".
- the cell voltage was 200 mV below the switch-off value and rose again to the same extent as before.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19853542234 DE3542234A1 (de) | 1985-11-29 | 1985-11-29 | Verfahren zur reinigung von kathoden bei der alkalichloridelektrolyse |
DE3542234 | 1985-11-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
EP0224790A1 true EP0224790A1 (de) | 1987-06-10 |
Family
ID=6287181
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19860115954 Withdrawn EP0224790A1 (de) | 1985-11-29 | 1986-11-18 | Verfahren zur Reinigung von Kathoden bei der Alkalichloridelektrolyse |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0224790A1 (fi) |
JP (1) | JPS62133096A (fi) |
DE (1) | DE3542234A1 (fi) |
FI (1) | FI864842A (fi) |
NO (1) | NO864508D0 (fi) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2020480A1 (de) * | 1970-04-27 | 1971-11-11 | Basf Ag | Verfahren zur Elektrolyse von Alkalichloriden |
US4174269A (en) * | 1978-06-21 | 1979-11-13 | Ppg Industries, Inc. | Method of treating electrodes |
EP0132816A1 (en) * | 1983-07-26 | 1985-02-13 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | A method for preventing degradation in activity of a low hydrogen overvoltage cathode |
EP0136794A2 (en) * | 1983-08-22 | 1985-04-10 | Imperial Chemical Industries Plc | Treatment of cathodes for use in electrolytic cell |
-
1985
- 1985-11-29 DE DE19853542234 patent/DE3542234A1/de not_active Withdrawn
-
1986
- 1986-11-12 NO NO864508A patent/NO864508D0/no unknown
- 1986-11-18 EP EP19860115954 patent/EP0224790A1/de not_active Withdrawn
- 1986-11-25 JP JP27889586A patent/JPS62133096A/ja active Pending
- 1986-11-27 FI FI864842A patent/FI864842A/fi not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2020480A1 (de) * | 1970-04-27 | 1971-11-11 | Basf Ag | Verfahren zur Elektrolyse von Alkalichloriden |
US4174269A (en) * | 1978-06-21 | 1979-11-13 | Ppg Industries, Inc. | Method of treating electrodes |
EP0132816A1 (en) * | 1983-07-26 | 1985-02-13 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | A method for preventing degradation in activity of a low hydrogen overvoltage cathode |
EP0136794A2 (en) * | 1983-08-22 | 1985-04-10 | Imperial Chemical Industries Plc | Treatment of cathodes for use in electrolytic cell |
Also Published As
Publication number | Publication date |
---|---|
DE3542234A1 (de) | 1987-06-04 |
FI864842A0 (fi) | 1986-11-27 |
NO864508D0 (no) | 1986-11-12 |
FI864842A (fi) | 1987-05-30 |
JPS62133096A (ja) | 1987-06-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE2818601C2 (fi) | ||
DE2912271A1 (de) | Verfahren und vorrichtung zur ueberfuehrung und reinigung von halogen und halogenwasserstoffsaeure in einem elektrochemischen system | |
EP0046522A1 (de) | Verfahren zum Regenerieren einer ammoniakalischen Ätzlösung | |
DE4243697C1 (de) | Elektrolytisches Verfahren zur Gewinnung von Platin hoher Reinheit aus Platinlegierungen | |
EP0224790A1 (de) | Verfahren zur Reinigung von Kathoden bei der Alkalichloridelektrolyse | |
DE2232903C3 (de) | Verfahren zur elektrolytischen Raffination von Kupfer unter Verwendung von Titanelektroden | |
DE3602683A1 (de) | Verfahren zur durchfuehrung der hcl-membranelektrolyse | |
DE19506242C2 (de) | Verfahren zur direkten elektrochemischen Oxidation von sulfithaltigen Lösungen, insbesondere Abwässern aus Gasreinigungsanlagen | |
DE4243699C1 (de) | Elektrolytisches Verfahren zur Gewinnung von Platin hoher Reinheit aus verunreinigtem Platin | |
DE2124045A1 (de) | Verfahren zur elektrolytischen Herstellung von reinem Chlor, Wasserstoff und reinen konzentrierten Alkaliphosphatlösungen und Elektrolysierzelle zur Durchführung des Verfahrens | |
DE1265153B (de) | Verfahren zur Herstellung von reinem Nickelhydroxyd | |
DE1240836B (de) | Anordnung zur Elektrolyse von Alkali-salzloesungen nach dem Amalgamverfahren und zurZersetzung des Amalgams | |
DE4108972A1 (de) | Verfahren zur erhoehung des molaren aluminium/chlor-verhaeltnisses | |
DE2304063A1 (de) | Verfahren zur reinigung von quecksilber | |
DE268816C (fi) | ||
DE460456C (de) | Verfahren zur elektrolytischen Raffination von Kupfer oder Kupferlegierungen unter Verwendung eines kupferchloruerhaltigen Elektrolyten | |
DE2856276C2 (de) | Verfahren zur Stromausbeutesteigerung einer Schmelzflußelektrolyse mit anodischer Sauerstoffentwicklung | |
EP0748396A1 (de) | Elektrolyseverfahren zum regenerieren einer eisen-iii-chlorid oder eisen-iii-sulfatlösung, insbesondere zum sprühätzen von stahl | |
DE588267C (de) | Verfahren zur Reinigung von Wasserstoffsuperoxydloesungen | |
DE2825011C2 (de) | Verfahren zur Ga-Rückgewinnung | |
AT226258B (de) | Verfahren zur Elektrolyse wässeriger Lösungen von Salzen amalgambildender Metalle an strömenden Quecksilberkathoden und Vorrichtung zur Durchführung des Verfahrens | |
DE752161C (de) | Elektrolyse von Alkalisulfatloesung | |
DE2745542A1 (de) | Verfahren zur elektrolyse von salzloesungen durch quecksilberkathoden | |
DE1141266B (de) | Verfahren und Vorrichtung zur Herstellung von Schwefelsaeure und Natronlauge durch elektrolytische Zersetzung einer waessrigen Natriumsulfatloesung | |
EP0126170B1 (de) | Verfahren und Vorrichtung zum Entfernen von SO2 aus SO2-haltigen Gasen |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19861118 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): BE DE FR GB IT NL SE |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN |
|
17Q | First examination report despatched |
Effective date: 19880504 |
|
18W | Application withdrawn |
Withdrawal date: 19880601 |
|
RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: MINZ, FRANZ-RUDOLF, DR. |