CN107475747A - A kind of method of the multiple new cupric electrolysis contact rod of low cost - Google Patents

A kind of method of the multiple new cupric electrolysis contact rod of low cost Download PDF

Info

Publication number
CN107475747A
CN107475747A CN201710629881.7A CN201710629881A CN107475747A CN 107475747 A CN107475747 A CN 107475747A CN 201710629881 A CN201710629881 A CN 201710629881A CN 107475747 A CN107475747 A CN 107475747A
Authority
CN
China
Prior art keywords
contact rod
low cost
multiple new
electrolysis
cupric electrolysis
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.)
Granted
Application number
CN201710629881.7A
Other languages
Chinese (zh)
Other versions
CN107475747B (en
Inventor
燕友全
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.)
DONGYING LUFANG METAL MATERIAL Co Ltd
SHANDONG FANGYUAN NONFERROUS METALS SCIENCE & TECHNOLOGY Co Ltd
DONGYING FANGYUAN NONFERROUS METALS Co Ltd
Original Assignee
DONGYING LUFANG METAL MATERIAL Co Ltd
SHANDONG FANGYUAN NONFERROUS METALS SCIENCE & TECHNOLOGY Co Ltd
DONGYING FANGYUAN NONFERROUS METALS 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 DONGYING LUFANG METAL MATERIAL Co Ltd, SHANDONG FANGYUAN NONFERROUS METALS SCIENCE & TECHNOLOGY Co Ltd, DONGYING FANGYUAN NONFERROUS METALS Co Ltd filed Critical DONGYING LUFANG METAL MATERIAL Co Ltd
Priority to CN201710629881.7A priority Critical patent/CN107475747B/en
Publication of CN107475747A publication Critical patent/CN107475747A/en
Application granted granted Critical
Publication of CN107475747B publication Critical patent/CN107475747B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/12Electrolytic production, recovery or refining of metals by electrolysis of solutions of copper
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/02Electrodes; Connections thereof
    • 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

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 Metals (AREA)

Abstract

The method that the present invention provides a kind of multiple new cupric electrolysis contact rod of low cost, including following steps:A. boil to scrapping contact rod and wash processing, make clean in appearance no-sundries;B. crack existing for scrapping contact rod surface is repaired, fine cracks are polished flat, compared with deep crack copper powder that its is floating;C. ear is tied up with copper wire to scrapping contact rod, tripping in electrolytic cell makes contact rod submerge in electrolyte, electrolysis a period of time as negative electrode;D. the contact rod completed will be electrolysed to take out from electrolytic cell, after flushing and finishing, that is, obtain again it is new after contact rod;Advantage is:Contact rod intensity increase after multiple reparation of the invention, conductive effect enhancing, Thinking Creation, methodological science are reasonable, and multiple new cost is low, efficiency high, realizes recycling for contact rod, has good economic benefit.

Description

A kind of method of the multiple new cupric electrolysis contact rod of low cost
Technical field
The present invention relates to non-ferrous metal field, and in particular to a kind of method of the multiple new cupric electrolysis contact rod of low cost.
Background technology
Contact rod primarily serves the effect of conduction during non-ferrous metal copper electrolyzing refining.All the time, there is coloured gold The contact rod that category industry cupric electrolysis workshop uses after a certain period of use time, the defects of surface can crack, pit, has and split Line, the contact rod of pit are easier by electrolytic corrosion, and electric conductivity is deteriorated, so annual cupric electrolysis industry has largely Contact rod due to crackle, pit is serious and scraps processing, this causes the waste of resource to a certain extent.
Contact rod used in prior art is solid, is made using copper-clad iron process, cost of manufacture is higher, but this conduction Rod intensity is big, is unlikely to deform, and can meet intensity requirement of the electrolysis production unit to contact rod.The service life of this contact rod is big About at 6 years or so, need to remake after reaching Rejection standard, and somewhat expensive.
The reason of scrapping of cupric electrolysis contact rod is mainly the corrosion in production process, mainly there is following several situations:(1)Lead Torch general corrosion, weight substantially mitigate, and weakened is yielding;(2)Contact rod surface corrosion is covered with fine cracks, conductive energy Power dies down;(3)Contact rod local corrosion is present compared with deep crack, and serious exposes internal iron staff, and iron, which enters electrolyte, can cause electricity Solve liquid pollution.
Cupric electrolysis workshop needs to buy new contact rod after contact rod is scrapped, and this undoubtedly adds the production of potroom Cost, and the disadvantage that contact rod has the wasting of resources to a certain extent is scrapped, do not meet current potroom cost efficiency Production requirement.
The content of the invention
It is an object of the invention to be solution the deficiencies in the prior art, and provide a kind of low cost multiple new cupric electrolysis contact rod Method.
The new technical scheme of the present invention is:A kind of method of the multiple new cupric electrolysis contact rod of low cost, comprises the following steps:
A. boil to scrapping contact rod and wash processing, make clean in appearance no-sundries;
B. crack existing for scrapping contact rod surface is repaired, fine cracks are polished flat, and are smeared compared with deep crack with copper powder It is flat;
C. ear is tied up with copper wire to scrapping contact rod, tripping in electrolytic cell makes contact rod be submerged after tying up ear in electrolyte, electricity as negative electrode Solution a period of time;
D. the contact rod completed will be electrolysed to take out from electrolytic cell, after flushing and finishing, that is, obtain again it is new after contact rod.
Contact rod is scrapped in the step a in the water that temperature is more than 90 DEG C, boils and is washed till surface
Redgreen and other no dirts.
Contact rod is tied up ear requirement copper wire and tied up away from contact rod termination about at 10cm in the step c.
The current strength of direct current is 10000A-16500A in the step c, and current density is
170-290A/m2
Bath composition is required in the step c(g/l):Cu2+45-55;H2SO4165-185;
Ni<15;Fe<3;Cl-0.03-0.07。
The temperature of electrolyte is 62-63 DEG C in the step c.
Electrolysis time in the step c, according to current strength size, adjustable range 10-18h,
According to discarded contact rod weight, electrolysis time is suitably increased or decreased.
The material of contact rod is configured to copper-clad iron contact rod, and beam conduction rod average weight is 4.8kg, scraps contact rod and puts down Equal weight is 4.3kg, and the contact rod average weight after answering newly is 5.1kg.
The beneficial effects of the invention are as follows:Innovative point of the present invention is to realize answering newly for cupric electrolysis contact rod, and advantage is to repair again Contact rod intensity increase after multiple, conductive effect enhancing, Thinking Creation, methodological science are reasonable, and multiple new cost is low, efficiency high, real Recycling for contact rod is showed, there is good economic benefit.
Brief description of the drawings
Fig. 1 is the process method flow chart of the present invention.
Fig. 2 is layout drawing of the multiple clean stub of the present invention in electrolytic cell.
Wherein:1 it is contact rod, 2 is that copper wire ties up ear.
Embodiment
The present invention will be further described below in conjunction with the accompanying drawings.
A kind of method of the multiple new cupric electrolysis contact rod of low cost, comprises the following steps:
A. boil to scrapping contact rod and wash processing, make clean in appearance no-sundries;
B. crack existing for scrapping contact rod surface is repaired, fine cracks are polished flat, and are smeared compared with deep crack with copper powder It is flat;
C. ear 2 is tied up with copper wire to scrapping contact rod, tripping in electrolytic cell makes contact rod be submerged after tying up ear in electrolyte as negative electrode, Electrolysis a period of time;
D. the contact rod 1 completed will be electrolysed to take out from electrolytic cell, after flushing and finishing, that is, obtain again it is new after contact rod 1.
Contact rod is scrapped in the step a in the water that temperature is more than 90 DEG C, boils and is washed till surface redgreen and without it His dirt.
Contact rod is tied up ear requirement copper wire and tied up away from the termination of contact rod 1 about at 10cm in the step c.
The current strength of direct current is 10000A-16500A, current density 170-290A/m2 in the step c.
Bath composition is required in the step c(g/l):Cu2+45-55;H2SO4165-185;Ni<15;Fe<3;Cl- 0.03-0.07。
The temperature of electrolyte is 62-63 DEG C in the step c.
Electrolysis time in the step c, according to current strength size, adjustable range 10-18h, according to discarded contact rod weight, Suitably increase or decrease electrolysis time.
The material of contact rod 1 is configured to copper-clad iron contact rod, and beam conduction rod average weight is 4.8kg, scraps contact rod Average weight is 4.3kg, and the average weight of contact rod 1 after answering newly is 5.1kg.
Case study on implementation:
Contact rod is scrapped as new object is answered using copper electrolyzing refining workshop, implementation steps are as follows:
A, contact rod will be scrapped to be placed in the water that temperature is more than 90 DEG C, boils and be washed till surface redgreen and without other dirts;
B, repaired to scrapping corrosive shake existing for the surface of contact rod, to scrapping contact rod surface difference corrosion condition Processing method, have following several:(1)Contact rod general corrosion, weight substantially mitigate, and surface crack is less, take measures be Directly prepare electrolysis;(2)There is more corrosive shake in contact rod integral surface, take measures to be to prepare electricity after surface is polished flat Solution;(3)Contact rod local corrosion exposes internal iron staff, it is with copper powder that the floating rear preparation in crack is electric to take measures compared with deep crack Solution;
C, as shown in Fig. 2 to scrapping after contact rod ties up ear 2 with copper wire, tripping in electrolytic cell is electrolysed as negative electrode, and anode is copper Positive plate.For ensure not influence to scrap contact rod it is new again after use, tie up ear status requirement away from scrapping conductive stick end about 10cm, Contact rod is scrapped in each cathode site energy tripping in 10, and electrolyte will be submerged by scrapping contact rod, and Faradaic current size is 15000A, It is electrolysed 16h;
D, the contact rod after the completion of electrolysis is taken out from electrolytic cell, the electrolyte on surface is rinsed out with water, to the long particle in surface Contact rod repaired with sanding machine, that is, obtain again it is new after contact rod.
It is 4.3kg to scrap contact rod in new preceding average weight again, and multiple new rear average weight is 5.1kg, passes through electrolysis, reports Useless contact rod surface adds one layer of copper, makes its surface smooth, and adds physical strength, enhances conductive effect, The use standard of potroom production is reached.
After contact rod input Workshop Production use after answering newly, the using effect of beam conduction rod is reached, it was demonstrated that make With method of the invention, it is possible to effectively multiple newly discarded contact rod, it is that cupric electrolysis production is cost-effective, increases the benefit.

Claims (8)

  1. A kind of 1. method of the multiple new cupric electrolysis contact rod of low cost, it is characterised in that:Comprise the following steps:
    A. boil to scrapping contact rod and wash processing, make clean in appearance no-sundries;
    B. crack existing for scrapping contact rod surface is repaired, fine cracks are polished flat, and are smeared compared with deep crack with copper powder It is flat;
    C. ear is tied up with copper wire to scrapping contact rod(2), tripping in electrolytic cell makes contact rod submerge electrolyte after tying up ear as negative electrode In, electrolysis a period of time;
    D. the contact rod completed will be electrolysed(1)Taken out from electrolytic cell, after flushing and finishing, that is, obtain again it is new after contact rod (1).
  2. A kind of 2. method of the multiple new cupric electrolysis contact rod of low cost according to claim 1, it is characterised in that:The step Contact rod is scrapped in a in the water that temperature is more than 90 DEG C, boils and is washed till surface redgreen and without other dirts.
  3. A kind of 3. method of the multiple new cupric electrolysis contact rod of low cost according to claim 1, it is characterised in that:The step Contact rod is tied up ear requirement copper wire and tied up away from contact rod in c(1)Termination is about at 10cm.
  4. A kind of 4. method of the multiple new cupric electrolysis contact rod of low cost according to claim 1, it is characterised in that:The step The current strength of direct current is 10000A-16500A, current density 170-290A/m2 in c.
  5. A kind of 5. method of the multiple new cupric electrolysis contact rod of low cost according to claim 1, it is characterised in that:The step Bath composition is required in c(g/l):Cu2+45-55;H2SO4165-185;Ni<15;Fe<3;Cl-0.03-0.07.
  6. A kind of 6. method of the multiple new cupric electrolysis contact rod of low cost according to claim 1, it is characterised in that:The step The temperature of electrolyte is 62-63 DEG C in c.
  7. A kind of 7. method of the multiple new cupric electrolysis contact rod of low cost according to claim 1, it is characterised in that:The step Electrolysis time in c, according to current strength size, adjustable range 10-18h, according to discarded contact rod weight, suitably increase or decrease electricity Solve the time.
  8. A kind of 8. method of the multiple new cupric electrolysis contact rod of low cost according to claim 1, it is characterised in that:Contact rod (1)Material be configured to copper-clad iron contact rod, beam conduction rod average weight is 4.8kg, scraps contact rod average weight and is 4.3kg, the contact rod after answering newly(1)Average weight is 5.1kg.
CN201710629881.7A 2017-07-28 2017-07-28 A kind of method of the multiple new cupric electrolysis conductive rod of low cost Active CN107475747B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710629881.7A CN107475747B (en) 2017-07-28 2017-07-28 A kind of method of the multiple new cupric electrolysis conductive rod of low cost

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710629881.7A CN107475747B (en) 2017-07-28 2017-07-28 A kind of method of the multiple new cupric electrolysis conductive rod of low cost

Publications (2)

Publication Number Publication Date
CN107475747A true CN107475747A (en) 2017-12-15
CN107475747B CN107475747B (en) 2018-10-09

Family

ID=60598277

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710629881.7A Active CN107475747B (en) 2017-07-28 2017-07-28 A kind of method of the multiple new cupric electrolysis conductive rod of low cost

Country Status (1)

Country Link
CN (1) CN107475747B (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101270483A (en) * 2007-03-22 2008-09-24 山西华圣铝业有限公司 Mending and ramming method for after reigniting electrolytic tank and clearing tank
JP2009114475A (en) * 2007-11-02 2009-05-28 Mitsui Mining & Smelting Co Ltd Electrode for producing electrolytic copper powder and anode for producing electrolytic copper powder
CN202174485U (en) * 2011-07-06 2012-03-28 湖南华洋铜业股份有限公司 Polishing device for copper current-conducting rod
CN104005042A (en) * 2014-06-06 2014-08-27 郴州市金贵银业股份有限公司 Method for antioxidation treatment of conducting rod in lead electrolysis system
CN203807572U (en) * 2014-02-28 2014-09-03 金川集团股份有限公司 Device for removing oxide layer of conductive rod on copper starting sheet
CN204587921U (en) * 2015-02-05 2015-08-26 中国有色(沈阳)冶金机械有限公司 A kind of contact rod feedway with contact rod clearing function
CN205856632U (en) * 2016-07-21 2017-01-04 金川集团股份有限公司 A kind of anode special purpose device for copper scap Direct Electrolysis
US20170058414A1 (en) * 2014-04-30 2017-03-02 Victor ARAYA BORQUEZ Insertable electrode device that does not generate acid mist or other gases, and method
CN106521562A (en) * 2016-09-30 2017-03-22 云南铜业股份有限公司 Recovery method of copper electrolysis permanent stainless steel cathode

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101270483A (en) * 2007-03-22 2008-09-24 山西华圣铝业有限公司 Mending and ramming method for after reigniting electrolytic tank and clearing tank
JP2009114475A (en) * 2007-11-02 2009-05-28 Mitsui Mining & Smelting Co Ltd Electrode for producing electrolytic copper powder and anode for producing electrolytic copper powder
CN202174485U (en) * 2011-07-06 2012-03-28 湖南华洋铜业股份有限公司 Polishing device for copper current-conducting rod
CN203807572U (en) * 2014-02-28 2014-09-03 金川集团股份有限公司 Device for removing oxide layer of conductive rod on copper starting sheet
US20170058414A1 (en) * 2014-04-30 2017-03-02 Victor ARAYA BORQUEZ Insertable electrode device that does not generate acid mist or other gases, and method
CN104005042A (en) * 2014-06-06 2014-08-27 郴州市金贵银业股份有限公司 Method for antioxidation treatment of conducting rod in lead electrolysis system
CN204587921U (en) * 2015-02-05 2015-08-26 中国有色(沈阳)冶金机械有限公司 A kind of contact rod feedway with contact rod clearing function
CN205856632U (en) * 2016-07-21 2017-01-04 金川集团股份有限公司 A kind of anode special purpose device for copper scap Direct Electrolysis
CN106521562A (en) * 2016-09-30 2017-03-22 云南铜业股份有限公司 Recovery method of copper electrolysis permanent stainless steel cathode

Also Published As

Publication number Publication date
CN107475747B (en) 2018-10-09

Similar Documents

Publication Publication Date Title
CN105624747B (en) A kind of copper/graphene composite multi-layer heat dissipation film
CN104131318B (en) A kind of CNT and/or Graphene strengthen lead base composite anode preparation method
CN101319333A (en) Titanium/aluminum composite board and production method thereof
CN107502945A (en) A kind of graphene aluminium alloy conductor and preparation method
WO2016086811A1 (en) Method for directly electrolyzing metal crushed aggregates
CN103668322B (en) A kind of steamalloy waste recovery copper, the method for nickel
CN109161890A (en) A kind of SiO2Differential arc oxidation composite coating and preparation method thereof
CN107475747B (en) A kind of method of the multiple new cupric electrolysis conductive rod of low cost
CN101817128A (en) Aluminum-based brazing filler metal with low melting point and preparation method thereof
CN106435263B (en) A kind of production method of the Pb-Ag-La alloy anode plates of energy-saving corrosion-resisting erosion
CN204455313U (en) Non-ferrous metal electrodeposition palisading type aluminium bar alloy lead anode plate
CN103789795B (en) A kind of anode steel claw for aluminum electrolysis
CN203639586U (en) Composite anode for hydrometallurgy
CN105220024B (en) A kind of electrowinning zinc negative electrode aluminium alloy and preparation method thereof
CN109594099A (en) A kind of direct current-carrying plate of novel graphene tri compound
CN204265867U (en) A kind of high-strength electrolytic zinc anode plate
CN102627002A (en) Preparation method of aluminum-base lead and lead alloy composite material
CN206882043U (en) A kind of electrode coating prosthetic device
CN203128675U (en) Cathode plate for electrolytic copper powder
CN205347602U (en) Electrodeposition is U type cylinder tubular water -cooling anode plate for metal
CN201354385Y (en) Aluminum electrolysis bath cathode block structure
CN105839142B (en) Aluminum electrolyzing cell used anode steel claw and preparation method thereof
CN110170634A (en) A kind of casting connection method of aluminium electrolysis prebaked anode carbon block and steel pawl
CN106319577A (en) Energy-saving and environment-friendly anode plate
CN210657213U (en) Steel strip electrolysis stripping tank

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
PP01 Preservation of patent right
PP01 Preservation of patent right

Effective date of registration: 20210721

Granted publication date: 20181009

PD01 Discharge of preservation of patent

Date of cancellation: 20240721

Granted publication date: 20181009