DE2729270A1 - Electrolyte recovery from rinsing baths in electroplating plant - by feeding rinsing water into plating tank fitted with evaporator - Google Patents
Electrolyte recovery from rinsing baths in electroplating plant - by feeding rinsing water into plating tank fitted with evaporatorInfo
- Publication number
- DE2729270A1 DE2729270A1 DE19772729270 DE2729270A DE2729270A1 DE 2729270 A1 DE2729270 A1 DE 2729270A1 DE 19772729270 DE19772729270 DE 19772729270 DE 2729270 A DE2729270 A DE 2729270A DE 2729270 A1 DE2729270 A1 DE 2729270A1
- Authority
- DE
- Germany
- Prior art keywords
- rinsing
- water
- electrolyte
- evaporator
- fed
- 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.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/16—Regeneration of process solutions
- C25D21/18—Regeneration of process solutions of electrolytes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
Description
Beschreibung und PatentansprücheDescription and claims
Bezeichnung: Verfahren zur Rückgewinnung von verschleppten Elektrolyten in galvanischen Anlagen.Designation: Process for the recovery of electrolytes that have been carried over in galvanic systems.
Anwendungsgebiet: Die Erfindung betrifft ein Verfahren bei dem mit Hilfe der Vakuum-Kühl technik in galvanischen Anlagen verschlepptes Elektrolyt rückgewonnen werden kann.Field of application: The invention relates to a method in which with With the help of vacuum cooling technology in electroplating systems, electrolyte that has been carried over is recovered can be.
Zweck der Erfindung: Beim austauchen der Ware aus einem galvanischen Bad bleibt an dieser Badflüssigkeit -Elektrolyt - haften und wird in das nachgeschaltete Spülbecken verschleppt. Um die steigende Konzentration in dem besagten Spülbecken in Grenzen zu halten, muß diesem Spülbecken laufend Frischwasser zugeführt und entsprechend mit Elektrolyt angereichertes Wasser abgeführt werden. Dieses Abwasser muß, bevor es in die Kanalisation geleitet wird, entgiftet und die Schadstoffe ausgefällt werden. Dieses heute noch übliche Verfahren ist umweltfeindlich und sehr kostspielig. Es erfordert nicht nur hohe Anlagenkosten für die Abwasser-Aufbereitungsanlage sondern auch beträchtliche Betriebskosten für die erforderlichen Aufbereitungs-Chemikalien. Hinzu kommt noch der laufende Frischwasserbedarf.Purpose of the invention: When the goods emerge from a galvanic The bath remains attached to this bath liquid - electrolyte - and is transferred to the downstream Sink carried away. About the increasing concentration in the said sink To keep within limits, fresh water must be continuously supplied to this sink and accordingly water enriched with electrolyte discharged will. This sewage must, before it is discharged into the sewer system, detoxified and the pollutants precipitated will. This process, which is still used today, is harmful to the environment and very expensive. It not only requires high plant costs for the wastewater treatment plant, but also also significant operating costs for the required treatment chemicals. In addition, there is the ongoing need for fresh water.
Aufgabe der Erfindung: Der Erfindung liegt die Aufgabe zugrunde, das verschleppte Elektrolyt den galvanischen Bädern wieder zuzuführen und gleichzeitig das Spüiwasser imKreislauf zu fahren.Object of the invention: The invention is based on the object that to supply the electrolyte carried over to the galvanic baths again and at the same time to circulate the flushing water.
Lösung: Diese Aufgabe wird erfindungsmäßig dadurch gelöst, daß 1. das Elektrolyt ständig über eine Vakuum-Verdampfungskühlanlage umgewälzt wird 2. das Spülwasser nicht wie bisher über die Abwasseraufbereitung in die Kanalisation sondern in das galvanische Bad geleitet wird 3. das verdunstete Wasser kondensiert und dem Spülbad zugeführt wird.Solution: According to the invention, this object is achieved in that 1. the electrolyte is constantly circulated through a vacuum evaporative cooling system 2. the rinsing water does not go into the sewage system via the wastewater treatment as before it is instead fed into the galvanic bath 3. the evaporated water condenses and fed to the rinsing bath.
Ein Ausführungsbeispiel der Erfindung ist in der Zeichnung dargestellt und wird im folgenden näher beschrieben: Die galvanisierte Ware verlässt das galvanische Bad (1) u d wird nacheinander in die Spülbader (2 und 3) getaucht. Hierbei ist die Anzahl der Spülbäder unerheblich. Im Gegenstrom hierzu wird das Spülwasser gepumpt, hierdurch nimmt die Elektrolytkonzentration von Bad zu Bad ab. Das überlaufende Spülwasser aus dem Spülbad (2) hat die höchste Elektrolytkonzentration und wird in das galvanische Bad zurückgepumpt. Mit diesem zurückgepumpten Spülwasser wird auch das verschleppte Elektrolyt dem galvanischen Bad wieder zugeführt. Das Elektrolyt aus dem galvanischen Bad (1) wird ständig über den Vakuum-Verdampfungskühler (4) und die Pumpe (5) umgewälzt. Im Vakuum-Verdampfungskühler (4) wird die Wassermenge verdunstet die dem galvanischen Bad (1) aus dem Spülbad (2) zugeführt wurde. Da hierbei dem Elektrolyt Verdainpfungswärme entzogen wird, kühlt sich dieses ab. Das dampfförmig entweichende Wasser wird im Kondensator (6) kondensiert und von der Pumpe (7) in das Spülbad (3) zurückgepumpt. Die Vakuum-Pumpe (8) saugt die Leckverluste ab. An embodiment of the invention is shown in the drawing and is described in more detail below: The galvanized goods leaves the galvanic bath (1) and enters the rinsing baths (2 and 3) one after the other submerged. The number of rinsing baths is irrelevant here. In countercurrent to this the rinsing water is pumped, this decreases the electrolyte concentration of the bath to bathroom off. The overflowing rinse water from the rinse bath (2) has the highest electrolyte concentration and is pumped back into the galvanic bath. With this rinse water pumped back the entrained electrolyte is also fed back into the electroplating bath. That Electrolyte from the electroplating bath (1) is continuously fed through the vacuum evaporative cooler (4) and the pump (5) circulated. The amount of water in the vacuum evaporation cooler (4) evaporates which was fed to the galvanic bath (1) from the rinsing bath (2). There If evaporation heat is withdrawn from the electrolyte, it cools down. That Water escaping in vapor form is condensed in the condenser (6) and from the Pump (7) pumped back into the rinsing bath (3). The vacuum pump (8) sucks in the leakage losses away.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19772729270 DE2729270B2 (en) | 1977-06-29 | 1977-06-29 | Method for recovering carried-over electrolyte |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19772729270 DE2729270B2 (en) | 1977-06-29 | 1977-06-29 | Method for recovering carried-over electrolyte |
Publications (2)
Publication Number | Publication Date |
---|---|
DE2729270A1 true DE2729270A1 (en) | 1979-01-04 |
DE2729270B2 DE2729270B2 (en) | 1980-06-12 |
Family
ID=6012644
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19772729270 Ceased DE2729270B2 (en) | 1977-06-29 | 1977-06-29 | Method for recovering carried-over electrolyte |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE2729270B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3634634A1 (en) * | 1985-10-11 | 1987-04-16 | Dominic Tenace | ELECTRIC PLATING SYSTEM |
US4781806A (en) * | 1985-10-11 | 1988-11-01 | Dominic Tenace | Electroplating system |
CN113737209A (en) * | 2021-09-27 | 2021-12-03 | 长江勘测规划设计研究有限责任公司 | Water electrolysis hydrogen production system adopting external circulation evaporation cooling full immersion and use method |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0132719B1 (en) * | 1983-07-30 | 1988-03-09 | Instytut Mechaniki Precyzyjnej | Method and device of conducting a closed cycle of the bath for plating of coatings |
-
1977
- 1977-06-29 DE DE19772729270 patent/DE2729270B2/en not_active Ceased
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3634634A1 (en) * | 1985-10-11 | 1987-04-16 | Dominic Tenace | ELECTRIC PLATING SYSTEM |
US4781806A (en) * | 1985-10-11 | 1988-11-01 | Dominic Tenace | Electroplating system |
CN113737209A (en) * | 2021-09-27 | 2021-12-03 | 长江勘测规划设计研究有限责任公司 | Water electrolysis hydrogen production system adopting external circulation evaporation cooling full immersion and use method |
Also Published As
Publication number | Publication date |
---|---|
DE2729270B2 (en) | 1980-06-12 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
OAP | Request for examination filed | ||
OD | Request for examination | ||
8235 | Patent refused |