CN205741227U - A kind of copper refining electrolysis bath of anode auto feed - Google Patents
A kind of copper refining electrolysis bath of anode auto feed Download PDFInfo
- Publication number
- CN205741227U CN205741227U CN201620682869.3U CN201620682869U CN205741227U CN 205741227 U CN205741227 U CN 205741227U CN 201620682869 U CN201620682869 U CN 201620682869U CN 205741227 U CN205741227 U CN 205741227U
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- Prior art keywords
- anode
- electrolyte
- shell fragment
- containing cavity
- electrolysis bath
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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Abstract
The utility model discloses the copper refining electrolysis bath of a kind of anode auto feed, including electrolyte containing cavity, the two ends of described electrolyte containing cavity are respectively arranged with rustless steel permanent cathode and blister copper plate anode, also include the shell fragment holding electrode being arranged in described electrolyte containing cavity, shell fragment clamping guide groove and be arranged at the anode suspension blowing wheel above described electrolyte containing cavity, described anode hangs and is provided with suspension blowing rope on blowing wheel, and the lower end of described suspension blowing rope is provided with the anode blowing for gripping described blister copper plate anode and accommodates head；Described shell fragment holding electrode is positioned at the lower section of described shell fragment clamping guide groove, and described blister copper plate anode clamps guide groove through described shell fragment.This utility model adopts the operation that progressively feeds in real time carrying out positive plate in an automated fashion, and not only operation labor intensity is low, working performance is high, and makes the liquid level in cathode copper refining electrolyzing cell easily controllable.
Description
Technical field
This utility model relates to a kind of cathode copper refinery practice equipment technical field, a kind of anode auto feed
Copper refining electrolysis bath.
Background technology
Cathode copper refinery practice is the blister copper that content copper amount is 99% to be made slab in advance make thin as anode, fine copper
Sheet makees negative electrode, using the mixed liquor of sulphuric acid and copper sulfate as electrolyte；After energising, the metallic copper element in blister copper is from anodic solution
Become copper ion to movable cathode, electronics will be obtained after arriving negative electrode and separate out cathode copper at negative electrode；Impurity in blister copper is main
For metallic elements such as active ferrum and zinc, the metallic element such as ferrum and zinc can be dissolved as metal ion with copper, due to ferrum
Difficult compared with copper ion with the foreign metal ion such as zinc separate out, as long as so during electrolysis suitably regulation potential difference can avoid ferrum and
The foreign metal ions such as zinc separate out on negative electrode；Additionally, possibly together with a small amount of impurity more inactive than copper such as gold and silver etc. in blister copper
The elements such as element, gold and silver can be deposited on the bottom of electrolysis bath and form the earth of positive pole.The fine copper that cathode copper refinery practice is produced
Plate is referred to as " cathode copper ", and the copper content in cathode copper is high, quality is good, may be used for manufacturing the excellence conductor of electric product.
Cathode copper refining electrolyzing cell of the prior art mainly uses intermission type artificial to add the mode of anode blister copper pole plate
Carrying out the charging operation of positive plate, above-mentioned operating type not only operation labor intensity is big, working performance is low, and can not realize sun
Progressively adding in real time of pole blister copper pole plate, makes the liquid level in cathode copper refining electrolyzing cell there is fluctuation, thus is not easy to realize electricity
Solve the automatically-monitored operation of liquid parameter.Therefore, it is necessary to design provide a kind of novel cathode copper refine electrolysis bath with gram
Take the problems referred to above.
Summary of the invention
In order to overcome the deficiencies in the prior art, this utility model provides the copper refining electrolysis of a kind of anode auto feed
Groove.
This utility model solves its technical problem and be the technical scheme is that
The copper refining electrolysis bath of a kind of anode auto feed, including electrolyte containing cavity, the two of described electrolyte containing cavity
End is respectively arranged with rustless steel permanent cathode and blister copper plate anode, also includes the Spring sheet clip being arranged in described electrolyte containing cavity
Holding electrode, shell fragment clamping guide groove and be arranged at the anode suspension blowing wheel above described electrolyte containing cavity, described anode hangs
Being provided with suspension blowing rope on blowing wheel, the lower end of described suspension blowing rope is provided with for gripping described blister copper plate
The anode blowing of anode accommodates head；Described shell fragment holding electrode is positioned at the lower section of described shell fragment clamping guide groove, described blister copper plate sun
Pole clamps guide groove through described shell fragment.
As the further improvement of technique scheme, the inwall of described electrolyte containing cavity includes electrolysis bath diapire and electricity
Solving groove sidewall, the height of described electrolysis bath diapire is by arranging one end of described rustless steel permanent cathode to arranging described blister copper plate sun
One end of pole is gradually lowered；Being provided with electrolyte Discharge outlet on described electrolysis bath diapire, described electrolyte Discharge outlet is arranged
One end in described blister copper plate anode place.
As the further improvement of technique scheme, the described electrolysis bath of one end of described rustless steel permanent cathode is set
It is additionally provided with electrolyte on sidewall and supplements charging spout；On the described cell sidewall of one end that described rustless steel permanent cathode is set
Being additionally provided with charging and put turbulent baffle, turbulent baffle is put in described charging and described cell sidewall surrounds formation electrolyte charging and leads to
Road, the upper end of described electrolyte loading channel connects described electrolyte and supplements charging spout, the lower end of described electrolyte loading channel
Connect described electrolyte containing cavity, and the lower end height of described electrolyte loading channel is less than described rustless steel permanent cathode and institute
State the lower end height of blister copper plate anode.
As the further improvement of technique scheme, it is that stainless steel material is made and described that turbulent baffle is put in described charging
The surface configuration of turbulent baffle is put in charging furane resins coat.
Compared with prior art, the beneficial effects of the utility model are:
The copper refining electrolysis bath of a kind of anode auto feed provided by the utility model, adopts and carries out sun in an automated fashion
The operation that progressively feeds in real time of pole plate, not only operation labor intensity is low, working performance is high, and in making cathode copper refining electrolyzing cell
Liquid level easily controllable, there is not bigger fluctuation, consequently facilitating realize the automatically-monitored operation of electrolyte parameter.
Accompanying drawing explanation
With embodiment, this utility model is further illustrated below in conjunction with the accompanying drawings.
Fig. 1 is the structural representation of the copper refining electrolysis bath of a kind of anode auto feed described in the utility model.
Detailed description of the invention
It is the structural representation of one specific embodiment of this utility model with reference to Fig. 1, Fig. 1.
As it is shown in figure 1, the copper refining electrolysis bath of a kind of anode auto feed, including electrolyte containing cavity 10, described electrolysis
The two ends of liquid containing cavity 10 are respectively arranged with rustless steel permanent cathode 11 and blister copper plate anode 12, it is characterised in that: also include setting
It is placed in the shell fragment holding electrode 21 in described electrolyte containing cavity 10, shell fragment clamps guide groove 22 and is arranged at described electrolyte and house
Anode above chamber 10 hangs blowing wheel 23, and described anode hangs and is provided with suspension blowing rope 24 on blowing wheel 23, described outstanding
The lower end hanging up material rope 24 is provided with the anode blowing blessing 25 for gripping described blister copper plate anode 12；Described bullet
Sheet holding electrode 21 is positioned at the lower section of described shell fragment clamping guide groove 22, and described blister copper plate anode 12 clamps guide groove through described shell fragment
22。
As preferably, the inwall of described electrolyte containing cavity 10 includes electrolysis bath diapire 13 and cell sidewall 14, institute
State the height of electrolysis bath diapire 13 by arranging one end of described rustless steel permanent cathode 11 to arranging described blister copper plate anode 12
One end is gradually lowered；Being provided with electrolyte Discharge outlet 15 on described electrolysis bath diapire 13, described electrolyte Discharge outlet 15 sets
It is placed in the one end at described blister copper plate anode 12 place.The described cell sidewall of one end of described rustless steel permanent cathode 11 is set
It is additionally provided with electrolyte on 14 and supplements charging spout 30；The described cell sidewall of one end of described rustless steel permanent cathode 11 is set
Being additionally provided with charging on 14 and put turbulent baffle 31, turbulent baffle 31 is put in described charging and described cell sidewall 14 surrounds formation electricity
Solving liquid loading channel 32, the upper end of described electrolyte loading channel 32 connects described electrolyte and supplements charging spout 30, described electrolysis
The lower end of liquid loading channel 32 connects described electrolyte containing cavity 10, and the lower end height of described electrolyte loading channel 32 is less than
Described rustless steel permanent cathode 11 and the lower end height of described blister copper plate anode 12.Described charging puts turbulent baffle 31 for rustless steel
Material is made and described charging is put the surface configuration of turbulent baffle 31 and had furane resins coat 33.
Described shell fragment clamping guide groove 22 is for the whereabouts attitude of blister copper plate anode 12 described in righting, described shell fragment holding electrode
21 for being energized to described blister copper plate anode 12, it is to avoid electric current causes the waste of energy consumption through the upper end of described blister copper plate anode 12
With；Arrange described charging put turbulent baffle 31 1 aspect can avoid supplement electrolyte time cause described rustless steel permanent cathode 11
And the electrolyte flow around described blister copper plate anode 12, affect the stability of electrolytic process parameter, on the other hand electrolyte from
Described electrolysis bath diapire 13 flows through the earth of positive pole that can rinse deposition, it is simple to the earth of positive pole is from described electrolyte loop exit 15 row
Go out.
Above preferable enforcement of the present utility model is illustrated, certainly, this utility model can also use with
The form that above-mentioned embodiment is different, those of ordinary skill in the art made on the premise of spirit of the present invention etc.
With conversion or change accordingly, all should belong in protection domain of the present utility model.
Claims (4)
1. a copper refining electrolysis bath for anode auto feed, including electrolyte containing cavity (10), described electrolyte containing cavity
(10) two ends are respectively arranged with rustless steel permanent cathode (11) and blister copper plate anode (12), it is characterised in that: also include arranging
Shell fragment holding electrode (21), shell fragment in described electrolyte containing cavity (10) clamp guide groove (22) and are arranged at described electrolyte
The anode of containing cavity (10) top hangs blowing wheel (23), and described anode hangs and is provided with suspension blowing rope on blowing wheel (23)
(24), the lower end of described suspension blowing rope (24) is provided with the anode blowing for gripping described blister copper plate anode (12)
Accommodate head (25)；Described shell fragment holding electrode (21) is positioned at the lower section of described shell fragment clamping guide groove (22), described blister copper plate anode
(12) through described shell fragment clamping guide groove (22).
The copper refining electrolysis bath of a kind of anode auto feed the most according to claim 1, it is characterised in that: described electrolyte
The inwall of containing cavity (10) includes electrolysis bath diapire (13) and cell sidewall (14), the height of described electrolysis bath diapire (13) by
The one end arranging described rustless steel permanent cathode (11) is gradually lowered to the one end arranging described blister copper plate anode (12)；Described electricity
Solving and be provided with electrolyte Discharge outlet (15) in groove bottom wall (13), described electrolyte Discharge outlet (15) is arranged at described blister copper plate
The one end at anode (12) place.
The copper refining electrolysis bath of a kind of anode auto feed the most according to claim 1, it is characterised in that: described in arranging not
It is additionally provided with electrolyte on the described cell sidewall (14) of one end of rust steel permanent cathode (11) and supplements charging spout (30)；Arrange
It is additionally provided with charging on the described cell sidewall (14) of one end of described rustless steel permanent cathode (11) and puts turbulent baffle (31),
Turbulent baffle (31) is put in described charging and described cell sidewall (14) surrounds formation electrolyte loading channel (32), described electrolysis
The upper end of liquid loading channel (32) connects described electrolyte and supplements charging spout (30), the lower end of described electrolyte loading channel (32)
Connect described electrolyte containing cavity (10), and the lower end height of described electrolyte loading channel (32) is permanent less than described rustless steel
Negative electrode (11) and the lower end height of described blister copper plate anode (12).
The copper refining electrolysis bath of a kind of anode auto feed the most according to claim 1, it is characterised in that: described charging is put
Turbulent baffle (31) is that stainless steel material is made and described charging is put the surface configuration of turbulent baffle (31) and had furane resins to coat
Layer (33).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620682869.3U CN205741227U (en) | 2016-07-02 | 2016-07-02 | A kind of copper refining electrolysis bath of anode auto feed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620682869.3U CN205741227U (en) | 2016-07-02 | 2016-07-02 | A kind of copper refining electrolysis bath of anode auto feed |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205741227U true CN205741227U (en) | 2016-11-30 |
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ID=57379284
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620682869.3U Expired - Fee Related CN205741227U (en) | 2016-07-02 | 2016-07-02 | A kind of copper refining electrolysis bath of anode auto feed |
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| CN (1) | CN205741227U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107268029A (en) * | 2017-06-30 | 2017-10-20 | 湘潭大学 | The method and apparatus that a kind of waterpower unloads the lead solution continuous electrolysis of lead |
| CN108866349A (en) * | 2018-08-09 | 2018-11-23 | 济源职业技术学院 | A kind of copper smelting by pyrometallurgy device |
-
2016
- 2016-07-02 CN CN201620682869.3U patent/CN205741227U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107268029A (en) * | 2017-06-30 | 2017-10-20 | 湘潭大学 | The method and apparatus that a kind of waterpower unloads the lead solution continuous electrolysis of lead |
| CN108866349A (en) * | 2018-08-09 | 2018-11-23 | 济源职业技术学院 | A kind of copper smelting by pyrometallurgy device |
| CN108866349B (en) * | 2018-08-09 | 2023-08-15 | 济源职业技术学院 | Fire copper smelting device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161130 Termination date: 20170702 |
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| CF01 | Termination of patent right due to non-payment of annual fee |