CN202099393U - Electrolytic recovery device - Google Patents

Electrolytic recovery device Download PDF

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Publication number
CN202099393U
CN202099393U CN2011201758437U CN201120175843U CN202099393U CN 202099393 U CN202099393 U CN 202099393U CN 2011201758437 U CN2011201758437 U CN 2011201758437U CN 201120175843 U CN201120175843 U CN 201120175843U CN 202099393 U CN202099393 U CN 202099393U
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CN
China
Prior art keywords
container
recovery device
electrolytic recovery
rotating shaft
water
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.)
Expired - Fee Related
Application number
CN2011201758437U
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Chinese (zh)
Inventor
张宏伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SUZHOU DINGSHANG SEAFOOD CO Ltd
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SUZHOU DINGSHANG SEAFOOD CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SUZHOU DINGSHANG SEAFOOD CO Ltd filed Critical SUZHOU DINGSHANG SEAFOOD CO Ltd
Priority to CN2011201758437U priority Critical patent/CN202099393U/en
Application granted granted Critical
Publication of CN202099393U publication Critical patent/CN202099393U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

The utility model aims to provide an electrolytic recovery device, which is used for treating cleaning water during the process of electroplating, extracting precious metal in the cleaning water, and clearing up cyanogen content in the cleaning water, and reduces the water treatment cost. The electrolytic recovery device comprises a container; a rotating shaft is mounted in the middle of a baseplate of the container in a penetrating manner; one or more metal plates serving as a cathode are mounted at the upper part of the rotating shaft; a metal object serving as an anode is arranged in the container; a water inlet and a water outlet are formed on the side wall of the container; the lower part of the rotating shaft is connected with a power device; the cathode is connected with the negative pole of a power source; and the anode is connected with the positive pole of the power source. The electrolytic recovery device has a simple structure and small volume, can be mounted with an electroplating assembly line in a matching manner directly, separates metal ion from the cleaning water in time to play a purifying role, reduces the cyanogen ions in the cleaning water and lowers the enterprise operation cost.

Description

A kind of electrolytic recovery device
Technical field
The utility model belongs to technical field of waste water processing, specially refers to a kind of rinse water that is used for handling in the electroplating process, or electroplating effluent, takes off the electrolytic recovery device of golden liquid.
Background technology
In plating line, contain toxic substances such as noble metal such as gold and cyanogen in its rinse water, therefore must could discharge after treatment, otherwise not only can cause the waste of noble metal, but also can cause serious environmental to pollute.Present rinse water treatment process is to handle through recovery and broken cyanide that ion exchange resin carries out noble metal, and is with high costs, and reusable edible not, and used resin can produce obnoxious flavour when reclaiming, and also can cause certain environmental pollution.
The utility model content
The purpose of the utility model is to propose a kind of electrolytic recovery device, is used for handling the rinse water in the electroplating process, extracts noble metal wherein, and removes cyanogen content wherein simultaneously, reduces cost of water treatment.
The electrolytic recovery device of the utility model comprises a container; Run through in the middle part of the base plate of said container a rotating shaft is installed; The top of said rotating shaft is equipped with one or more metal sheets of useing negative electrode as; Also be provided with in the said container and use the anodic metal object as, the sidewall of said container has water-in and water outlet; The bottom of said rotating shaft links to each other with PWR PLT; Said negative electrode with link to each other with the negative pole of power supply, said anode links to each other with the positive pole of power supply.
According to electrolytic principle; After containing the rinse water entering container of precious metal ions such as gold, its metals ion can be attached to cathode surface under the effect of electrode, simultaneously because electric current itself have the effect of heating; Can heat rinse water, so just can crack the cyanogen in the water.Use after for some time, just can reclaim noble metal as long as change the metal sheet of useing negative electrode as.In addition, metal sheet can rotate under the effect of rotating shaft and PWR PLT, and the rinse water in the container is formed stirring action, accelerates the separation of metals ion.
Further, the said metal sheet of useing negative electrode as is that pure titanium metal is processed, and in electrolytic process, need not to add any electrolysis promotor, to the quality not influence fully of liquid bath water quality and product.
Further, said water-in is arranged at the bottom of wall of container, and said water outlet is arranged at the top of wall of container.Like this rinse water can be from the bottom to top overflow container gradually, can guarantee the metals ion in the rinse water is separated absorption in the process the inside of overflowing.
Further, said container is processed for the PVC material.Because rinse water is mordant, therefore adopt protection against corrosion, insulation, resistant to elevated temperatures PVC material is made container can guarantee safety.
Further, said PWR PLT are the buncher that is installed on the container below, and said buncher is connected with said rotating shaft through belt.To different rinse water, can control the velocity of separation of precious metal ion through the rotating speed of regulating buncher.
Further, the said anodic metal object of useing as is for around rotating shaft and use the metallic cylinder of the metal sheet of negative electrode as.Adopt metallic cylinder as anode, can enlarge the anodic area as much as possible, thereby improve the separation rate of precious metal ion.
Further, PL, the switch that is used for control electrode work, the PL that is used to indicate the PWR PLT working order that is used for the indicator electrode working order, the switch that is used to control PWR PLT work are installed on the said container outside wall.Above-mentioned switch and PL are set can be helped to control the carrying out of electrolysis work and observe working order.
Further, said water inlet is equipped with adverse current and suppresses valve, to prevent the aqueous reflux in the container.
The electrolytic recovery apparatus structure of the utility model is simple, and volume is little, can be directly and the supporting installation of plating line; Metals ion in the rinse water is separated timely; Play Water purification, reduce the cryanide ion in the rinse water simultaneously, reduce the cost of enterprise operation.
Description of drawings
Fig. 1 is the structural representation of the electrolytic recovery device of the utility model.
The time dependent synoptic diagram of residual gold concentration when Fig. 2 is to use the electrolytic recovery device of the utility model in the rinse water.
The synoptic diagram of the residual cyanogen concentration changes with time when Fig. 3 is to use the electrolytic recovery device of the utility model in the rinse water.
Indicate among the figure: 1, container; 2, rotating shaft; 3, pure titanium metal plate; 4, metallic cylinder; 5, water-in; 6, water outlet; 7, belt; 8, buncher.
Embodiment
Contrast accompanying drawing below; Through description, the effect of the mutual alignment between the shape of the embodiment of the utility model such as related each member, structure, the each several part and annexation, each several part and principle of work etc. are done further to specify to embodiment.
Embodiment 1:
As shown in Figure 1; The electrolytic recovery device of present embodiment comprises the container 1 that a PVC material is processed; The base plate of container 1 middle part is run through a rotating shaft 2 being installed, and the top of rotating shaft 2 is equipped with four pure titanium metal plates 3 of useing negative electrode as, also is provided with in the container 1 around rotating shaft 2 and the metallic cylinder 4 of pure titanium metal plate 3 of useing negative electrode as to use anode as; The lower sidewall of container 1 has water-in 5, and top has water outlet 6; The bottom of rotating shaft 2 links to each other with a buncher 8 that is installed on the container below through belt 7; Pure titanium metal plate 3 with link to each other with the negative pole of power supply, metallic cylinder 4 links to each other with the positive pole of power supply; The switch that PL, the switch that is used for control electrode work, the PL that is used to indicate the PWR PLT working order that are used for the indicator electrode working order is installed on container 1 outer side wall, is used to control PWR PLT work (figure do not draw power supply, switch, PL).
Further, said water inlet is equipped with adverse current and suppresses valve, to prevent the aqueous reflux (adverse current of not drawing among the figure suppresses valve) in the container.
Like Fig. 2, shown in 3, after using the electrolytic recovery device of present embodiment, the growth that residual gold concentration in the rinse water and residual cyanogen concentration can be in time and significantly reducing.
In use, in the accumulator tank of plating line, wherein water pump will be installed by water inlet pipeline place with water outlet pipeline and water inlet pipe connection.Confirm whether reclaim liquid in the accumulator tank, can not start shooting when not reclaiming liquid then.
Concrete steps are following: A, open the pump operation switch; B: open electrode supply running switch; C: regulate motor speed as required; D: after using for some time, pull down and change the pure titanium metal plate 3 of useing negative electrode as, reclaim metal.
With a circuit board plant is example, and the gold-plated flow line of the soft board of this circuit board plant has been installed the electrolytic recovery device of two playscript with stage directions embodiment.Before the electrolytic recovery device was installed, draining weekly contained golden waste water 1600kg, contained gold amount 1200 grams, and every month near the 5kg flight of gold; Rinse water is changed once weekly at least, 500 yuan/ton of its broken cyanide expenses.
After using the electrolytic recovery device, reclaimed 5kg gold in every month, rinse water is by original changing into biweekly once in a week, and the broken cyanide expense reduces 2/3rds.
Through above-mentioned instance explanation, the electrolytic recovery device of present embodiment has reduced a large sum of running cost for enterprise really.

Claims (8)

1. electrolytic recovery device; It is characterized in that comprising a container; Run through in the middle part of the base plate of said container a rotating shaft is installed; The top of said rotating shaft is equipped with one or more metal sheets of useing negative electrode as, also is provided with in the said container to use the anodic metal object as, and the sidewall of said container has water-in and water outlet; The bottom of said rotating shaft links to each other with PWR PLT; Said negative electrode with link to each other with the negative pole of power supply, said anode links to each other with the positive pole of power supply.
2. electrolytic recovery device according to claim 1 is characterized in that the said metal sheet of useing negative electrode as is that pure titanium metal is processed.
3. electrolytic recovery device according to claim 1 and 2 is characterized in that said water-in is arranged at the bottom of wall of container, and said water outlet is arranged at the top of wall of container.
4. electrolytic recovery device according to claim 1 and 2 is characterized in that said container is PVC, and the PP material is processed.
5. electrolytic recovery device according to claim 1 and 2 is characterized in that said PWR PLT are the buncher that is installed on the container below, and said buncher is connected with said rotating shaft through belt.
6. electrolytic recovery device according to claim 1 and 2 is characterized in that the said anodic metal object of useing as is for around rotating shaft and use the metallic cylinder of the metal sheet of negative electrode as.
7. electrolytic recovery device according to claim 1 and 2 is characterized in that being equipped with on the said container outside wall PL, the switch that is used for control electrode work, the PL that is used to indicate the PWR PLT working order that is used for the indicator electrode working order, the switch that is used to control PWR PLT work.
8. electrolytic recovery device according to claim 1 and 2 is characterized in that said water inlet is equipped with adverse current and suppresses valve.
CN2011201758437U 2011-05-30 2011-05-30 Electrolytic recovery device Expired - Fee Related CN202099393U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011201758437U CN202099393U (en) 2011-05-30 2011-05-30 Electrolytic recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011201758437U CN202099393U (en) 2011-05-30 2011-05-30 Electrolytic recovery device

Publications (1)

Publication Number Publication Date
CN202099393U true CN202099393U (en) 2012-01-04

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Application Number Title Priority Date Filing Date
CN2011201758437U Expired - Fee Related CN202099393U (en) 2011-05-30 2011-05-30 Electrolytic recovery device

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CN (1) CN202099393U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102808200A (en) * 2011-05-30 2012-12-05 苏州市鼎尚海珍品有限公司 Electrolysis recovery apparatus
CN111302541A (en) * 2020-03-23 2020-06-19 上海与非日用品有限公司 Open-air simple and easy water purifier based on water conservancy

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102808200A (en) * 2011-05-30 2012-12-05 苏州市鼎尚海珍品有限公司 Electrolysis recovery apparatus
CN111302541A (en) * 2020-03-23 2020-06-19 上海与非日用品有限公司 Open-air simple and easy water purifier based on water conservancy

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120104

Termination date: 20120530