GB2040311A - Cathode for use in the electrolytic refining of copper - Google Patents

Cathode for use in the electrolytic refining of copper Download PDF

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Publication number
GB2040311A
GB2040311A GB8002075A GB8002075A GB2040311A GB 2040311 A GB2040311 A GB 2040311A GB 8002075 A GB8002075 A GB 8002075A GB 8002075 A GB8002075 A GB 8002075A GB 2040311 A GB2040311 A GB 2040311A
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sheet
copper
starter
cathode
cathode according
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GB2040311B (en
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Copper Refineries Pty Ltd
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Copper Refineries Pty Ltd
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    • 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

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  • 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 cathode comprises a stainless steel hanger bar 11 having a flat undersurface 12 with end portions 13 adapted to rest upon supports and electrical contacts, a flat stainless steel starter sheet 14 welded by its upper edge to the undersurface 12 between the end portions 13 so as to extend perpendicularly from said undersurface, the bar 12 and at least the marginal upper portion of the sheet 14 by which it is welded to the under-surface 12 of the bar being clad (e.g. plated) with copper as represented by the stippling. At least the upright side edges of the sheet 14 carrying masking 18. <IMAGE>

Description

SPECIFICATION Cathode for use in the electrolytic refining of copper This invention relates to cathodes for use in the electrolytic refining of copper.
For over fifty years and up to the present the most commonly used cathode of the type in question has been in the form illustrated, by way of a perspective sketch, in Figure 1 of the drawings herewith. Neither Figure 1 nor Figure 2 (referred to later herein) are drawn to scale, having certain parts disproportionately enlarged so as more clearly to illustrate the details of construction.
Referring to Figure 1, the prior art cathode consists of a copper hanger bar 7, a copper starter sheet 8 and a pair of copper loops or straps 9 by which the sheet is hung on the bar. The end portions 10 of bar 7 project beyond the width of sheet 8 so that they may rest, for support, on the cell sides with one making the usual electrical contact, and with the starter sheet between a pair of anode plates of unrefined copper, both being immersed in the electrolyte of a refining cell, or between a pair of insoluble anodes both immersed in the electrolyte of an electro-winning cell.
Notwithstanding their long use in the industry, it is well recognised that the prior cathodes are open to objection in several respects. For example: (a) The copper starter sheets are not re-usable. That is to say, they cannot be stripped of the copper deposited on them and then put back in the cell to receive a fresh copper deposit. The present and most economical practice is to melt the starter sheet copper, along with the copper deposited on it, and from the melt produce wirebars, rod, cakes, billets and other copper stock commodities in marketable condition.A fraction of the melt output could be used for making fresh starter sheets, experience has shown however that it is more economic to produce fresh starter sheets electrolytically; but even so, the man-hour expenditure is extremely high because it involves stripping of starter sheets from mother plates, flattening of sheets, making and attaching the loops, and assembly of the looped sheets with support bars.
(b) The copper starter sheets are not easily made truly flat and even when they are substantially flat to start with they frequently warp in service and this gives rise to short circuiting between cathode and anode.
Even where loss of flatness is not as bad as that, any departure from parallelism between cathode and anode causes non-uniformity of copper deposit, with excess deposit at "peak" or short-path points accelerating short circuiting at those points. Short circuiting is a serious problem in that it is necessary to use a team of men whose task consists entirely of patrolling the tank-house to remedy short circuits.
(c) Sometimes the loops 9 make little more than line, or even point, contact with the support bar 7. This does not impair the actual copper deposit process, but it does increase resistance and consequently power costs are increased.
Extensive research and experiment have been carried out in the copper refining industry to improve the mother plate from which the starting sheets are produced. Some work was done with stainless steel but was generally unsuccessful due to inconsistency in results which gave problems such as passivity, localised corrosion and variable adhesion of the copper deposits.
Titanium starter blanks have had considerable acceptance because of the inherent characteristics of titanium which provide an oxide film which appears well suited to overcoming the problems of too little or too much adhesion of the copper deposit and its corrosion resistance is exceptionally good. The most advanced form of titanium re-usable starter plate or cathode is complex in consisting of a composite hanger bar primarily composed of copper and incorporating a titanium component to which a titanium starter plate is welded. In one form, the hanger bar is a copper bar encased in a titanium shell and the top marginal portion of the starter plate is goose-necked so that that portion may be welded directly to one side of the hanger bar encasement. In another form the hanger bar is a copper bar having a core rod of titanium inside and running longitudinally of it.In this case, the starter plate is goose-necked as before and is welded to the core rod by way of short studs of titanium which extend through holes in the copper bar, each stud having one end welded to the core rod and its other end welded to the starter sheet margin.
An example of the prior "titanium" arrangement just described is provided by that subject of United Kingdom Patent 1415793.
However, titanium is not without its shortcomings. It is expensive and its production in a practical form is complicated. The original object of the present invention was to overcome or ameliorate at least some of the mentioned shortcomings and in a preferred embodiment, all of those shortcomings, in a particularly simple and inexpensive manner by the provision of a cathode which is virtually entirely of stainless steel, is indefinitely re-usable, maintains its flatness, provides an unimpaired current path between bus-bar and hanger bar and between that bar and the plate, provides a permanent oxide coating acting as an effective parting layer facilitating stripping of deposit copper from the starter blank while providing sufficient adhesion for retention of deposited copper during build-up, and is particularly amenable to mechanical handling in its manufacture and use.
Experimental use of invention has proved so successful that it is considered economic to extend the use of this cathode throughout applicants electrolytic copper refining tank house.
The conventional method of refining makes use of starter blanks in a limited number of cells to produce two thin sheets of refined copper from each plate each day. These sheets are then assembled into the cathode as shown in Figure 1.
The special starter sheet manufacturing operation involving additional control, higher power consumption per tonne of product, and considerable expenditure on labour can be eliminated by the use of the present invention in all cells and for a longer time growth (a week or more instead of only 24 hours) before stripping.
It also provides a suitable electrode for mechanical handling and mechanical stripping of which the product is commercial refined cathode copper.
In addition the accurate dimensions of the starter blank, when coupled with accurately dimensioned anodes, provide the facility to operate at closer spacing of electrodes thereby considerably reducing power costs, and most importantly largely eliminating short circuits, thus further reducing labour costs and offering a better facility for computer monitoring of short circuits. Furthermore the more intensive operation made possible with closer spacing, and the higher current density at which the refining operation can be performed because of the elimination of short circuits, means that the plant for a given annual capacity can be housed in a smaller building, thus offering considerable savings in capital investment for that building.
The elimination of starter sheets and their requirement of special, larger area, anodes and particularly the ability to take more "pulls" from a loading of anodes all reduce the amount of "working" copper in the process at any time. As this reduction can be of the order of 20% of say 10,000 tonnes, the amount of money invested in the copper in process is considerably reduced.
The invention provides a cathode for use in the electrolyte refining of copper, comprising: A stainless steel hanger bar having a flat undersurface with end portions adapted to rest upon supports and electrical contacts.
A flat stainless steel starter sheet welded by its upper edge to said undersurface between said end portions and so asto extend perpendicularly from said undersurface, a copper cladding which envelops said bar and at least the marginal upper portion of said sheet by which it is welded to said undersurface, and means to mask at least the upright side edges of said sheet.
It will be appreciated that terms used herein, such as "undersurface", "upper edge" and others implying a specific orientation for a cathode or the parts thereof, are used for descriptive convenience. Such terms are literally appiicable to a cathode when in normal use suspended in an electrolytic cell.
A preferred embodiment of the invention is illustrated in Figures 2 to 6 of the drawings herewith.
Figure 2 is a perspective view of a cathode not drawn to scale as previously explained.
Figure 3 is a side elevation of the same cathode when drawn to a presently preferred scale.
Figure 4 is an end elevation projected from Figure 3.
Figure 5 repeats, on a enlarged scale, that part of Figure 4 enclosed by circle 5.
Figure 6 is a section taken on line 6-6 on a still further enlarged scale.
Referring to Figures 2 to 6, a stainless steel hanger bar 11 is preferably of RSJ or I-beam cross-sectional shape as shown. It could be of some other shape, but that shown is preferred because it is of light weight and hence economical of the steel employed, it is structurally sound and it provides a relatively large surface area for the current to be transmitted. Bar 11 has a flat undersurface 12 and end portions 13 adapted to rest on support and electrical contacts as well understood.
A flat stainless steel starter sheet 14 is welded, as indicated at 15 in Figure 5, by its upper edge to undersurface 12so that the sheet extends perpendicularly from the undersurface 12. Sheet 14 preferably has a pair of holes 16 gapped from it prior to welding. These holes facilitate mass handling of a number of the cathodes by support rods or prongs extended through the holes.
A range of stainless steels may serve effectively as starter plates according hereto, for ease of copper stripping howeve we prefer to use that grade of stainless steel marketed as "AISI 316 ELC" and having what is known as a "2B" standard of surface finish. This steel is one having an approximate analysis of: Carbon 0.03% by weight Nickel 12.0% by weight Chromium 17.0% by weight Molybdenum 2.25% by weight and the 2B surface finish is one intermediate bright and dull, being a silvery-grey, semi-bright surface produced by cold rolling, softening and descaling, and then final rolling lightly with polished rolls.
The indicated steel and surface finish are preferred, as experiment has shown that they provide a sufficient tenacity of attachment between the steel sheet and the copper deposited therein to prevent the copper from peeling or slumping from the steel on its own accord; yet, this tenacity is not such as to impede ready stripping of the copper from the steel sheet. Stripping may be performed by use of knife-like blades or knife-edge wedges inserted between the steel sheet and the deposited copper at the upper edge of the copper; however, using stainless steel of the kind and surface finish indicated above, our experiments have shown that effective stripping may be carried out automatically by passing the copper laden cathodes through a hammering station in which the deposited copper is smartly rapped near its upper edge from both sides, this loosens the copper upper edge and stripping is then finished by directing one or more streams of air into the minute space between the steel and the loosened upper edge of the copper.
The stainless steel out of which the hanger bar is made may be the same as that from which the starter sheet is made. The bar may however, by of any other stainless steel provided it is one to which the sheet is weldable.
As previously mentioned herein, stainless steel is not a particularly good conductor, and use of a hanger bar made only of such steel is not a sufficient vehicle for passage of current between bus-bar and starter sheet. We have found that this can be overcome by simply cladding the hanger bar, and a top margin of the sheet welded to it, with copper. This cladding may be applied by published techniques of plating and a thickness of about 1 m.m. is preferred to provide adequate electrical conductivity and the ability to withstand corrosion and machanical drainage. It will be recalled that earlier herein the presence of an oxide film on the starter plate is regarded as desirable owing to its ability to act as a parting layer to facilitate stripping of copper from the sheet.
The width of the copper plated margin at the top of the starter sheet is not critical provided it stops short of the top surface of the electrolyte. Obviously, deposit of copper on the plating area must not occur. Similarly, the plating area on which refined copper will be deposited in the operating process must not extend onto the lower edges 17 defining holes 16. It follows, that the copper plating may conveniently stop short of the edges 17 provided it covers the (preferably sand-blasted) weld metal at 15.
It will be apparent that ease of copper stripping requires effective masking of the starter sheet edges so that the deposit of copper will not be continuous about those edges. This is particularly the case with the upright side edges of the plate. The bottom edge is less in need of maskng and in the case of that edge masking could be omitted; however, to improve assurance of clean stripping we prefer to mask the bottom edge merely by giving it a hot dip, to a depth of about 10.00 mm, of a high melting point resilient wax, or other masking material.
With regard to masking of the side edges of the starter sheet the present invention displays a further important advantage over the titanium sheets referred to previously herein.
In titanium starter sheets, owing to the relatively high conductivity of that metal, there is a proneness for creep of deposit copper particles under the masking strip material. Once that happens copper nodules continue to grow under the mask strip (usually of plastics material) thus tending to lift the strip and so defeat the reason for masking and also create the need for re-masking before further use.
With stainless steel starter sheets, the relatively poor conductivity discourages copper growth under the masking means and such growth is thereby reduced to such a degree as to become inconsequential.
Notwithstanding this, the desirability of effective masking of at least the side edges of the starter sheet remains; and, for preference, the form of masking which we employ is as shown best in Figure 6.
Referring mainly to that figure, the masking means comprise a longitudinally slotted plastics beading 18 held on to the sheet 14 by plastics pins 19. These pins extend through holes 20 formed in plate 14.
The beading 18 and the pins 19 are preferably made of the same plastics material, and one suitable material is a high quality, heat and impact resistant plastic such as that known as CYCOLOY 800. This being a polymeric alloy of acrylonitrile-butadiene-styrene, (ABS) and polycarbonate as described inU. S. patent 3,130,177.
The beading 18 and the pins 19 are secured together by use of a suitable bonding material such as a 30% solution of Cycoloy 800 in methylene chloride.
Such a bonding material sets to an elastic condition and in addition to acting as a bonding agent it serves a useful purpose in the following manner.
During the experimentation which led up to the present invention it was found that on some occasions there was a tendency for the applied beadings to slightly bulge between the pin fastenings. This was, of course, objectionable and it was considered to be due to difference in expansion rates between the steel and the beading. This situation was remedied by making the holes 20 oversized as shown in Figure 6. In applying the beadings and the pins the holes 20 are filled by the solvent material which sets to an elastic condition so to act as expansion joints permitting sufficient longitudinal movement of the beading relative to the starter sheet as will compensate for the expansion rate difference.
The beadings 18 are preferably first formed by extrusion, or injection moulding, and in this action it is desirable for the points 21 defining the aperture of slot 22 to be placed closer to each other than is shown in Figure 6. Thus, when the beading is applied to the sheet, the sides of the slot 22 have an inbuilt resilient loading tending to press them firmly in contact with the sheet.
As a further precaution the points 21 are preferably sealed relative to the starter sheet by the application of wax or other material sealing strips as indicated at 23.

Claims (11)

1. A cathode for use in the electrolytic refining of copper, comprising: a stainless steel hanger bar having a flat undersurface with end portions adapted to rest upon supports and electrical contacts, a flat stainless steel starter sheet welded by its upper edge to said undersurface between said end portions and so as to extend perpendicularly from said undersurface, a copper cladding which envelopes said bar and at least the marginal upper portion of said sheet by which it is welded to said undersurface, and means to mask at least the upright side edges of said sheet.
2. A cathode according to claim 1 wherein said hanger bar is of I-beam cross-sectional shape.
3. A cathode according to claim 1 or claim 2 wherein said starter sheet has lifting holes formed in it as gaps in that edge of the sheet by which the sheet is welded to said hanger bar.
4. A cathode according to any one of the preceding claims wherein said starter sheet is formed of stainless steel containing: Carbon 0.03% by weight Nickel 12.0% by weight Chromium 17.0% by weight Molybdenum 2.25% by weight
5. A cathode according to any one of the preceding claims wherein said copper cladding is formed by platig.
6. A cathode according to any one of the preceding claims wherein said masking means comprise plastics beadings each having a longitudinal slot by which the beading embraces the sheet, and a plurality of plastics pins extending through holes formed in said sheet and having those portions of them disposed on either side of said slot bonded within said beading.
7. A cathode according to claim 6 wherein said beading is so formed by extrusion and said pins are so applied thereto that the sides of said slot are resiliently loaded to bear firmly against a starter sheet portion placed therebetween.
8. A cathode according to claim 6 or claim 7 wherein the holes in said sheet to receive said pins are over-sized relative to said pins and the open space thus created is filled with elastic solvent material so that each of the joints established by said pins constitutes an expansion joint.
9. A cathode according to any one of claims 6 to 8 wherein said masking means include wax strips by which the interior of said slot is sealed in relation to that portion of the starter sheet inserted in said slot.
10. A cathode according to any one of the preceding claims wherein the lower edge of said sheet is masked by a coating of a hight-melting point, resilient wax applied thereto.
11. A cathode for use in the electrolytic refining of copper substantially as herein described with reference to Figures 2 to 6 of the drawings herewith.
GB8002075A 1979-02-05 1980-01-22 Cathode for use in the electrolytic refining of copper Expired GB2040311B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AU43909/79A AU506521B1 (en) 1979-02-05 1979-02-05 Cathode with stainless steel - copper clad hanger bar

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GB2040311A true GB2040311A (en) 1980-08-28
GB2040311B GB2040311B (en) 1983-02-09

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JP (1) JPS5943996B2 (en)
AU (1) AU506521B1 (en)
BE (1) BE881500A (en)
BR (1) BR8000692A (en)
CA (1) CA1150669A (en)
DE (1) DE3003927C2 (en)
ES (1) ES8103198A1 (en)
FI (1) FI68430C (en)
GB (1) GB2040311B (en)
MX (1) MX155943A (en)
MY (1) MY8400147A (en)
PH (1) PH17223A (en)
PL (1) PL123151B1 (en)
SE (1) SE445050B (en)
SU (1) SU1344252A3 (en)
YU (1) YU42960B (en)
ZA (1) ZA80341B (en)
ZM (1) ZM1480A1 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4670124A (en) * 1985-08-31 1987-06-02 Norddeutsche Affinerie Aktiengesellschaft Cathode for use in the electrolytic refining of copper and method of making same
US4882027A (en) * 1986-02-06 1989-11-21 Kidd Creek Mines Ltd. Cathode hangers
EP0454056A1 (en) * 1990-04-23 1991-10-30 Austria Metall Aktiengesellschaft Aluminium cathode-plate for the electrowinning of zinc
WO2003031692A2 (en) * 2001-10-02 2003-04-17 Norddeutsche Affinerie Aktiengesellschaft Electrolysis cathode
EP1428910A1 (en) * 2002-12-13 2004-06-16 Paul Wurth S.A. Method For Converting An Electrorefinery And Device For Use Therein
WO2008099057A1 (en) * 2007-02-13 2008-08-21 Outotec Oyj Method of manufacturing a cathode plate, and a cathode plate
US8038855B2 (en) 2009-04-29 2011-10-18 Freeport-Mcmoran Corporation Anode structure for copper electrowinning
CN103726076A (en) * 2005-03-09 2014-04-16 斯特拉塔昆士兰有限公司 Stainless steel electrolytic plate

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2104549B (en) * 1981-08-26 1984-12-12 Copper Refineries Pty Ltd Cathode for use in the electrolytic refining of copper
IT1152776B (en) * 1982-05-27 1987-01-14 Snam Progetti INSOLUBLE ANODES FOR THE EXTRACTION OF THE LEAD FROM THE ELECTROLYTE IN THE ELECTROCHEMICAL PROCESSES FOR THE RECOVERY OF THE METALS CONTAINED IN THE EXHAUSTED ACCUMULATORS
JPS6393884A (en) * 1986-10-09 1988-04-25 Nippon Mining Co Ltd Electrolysis method
DE4241485C1 (en) * 1992-12-09 1994-03-17 Siemens Ag Cathode for copper@ electrorefining or electrowinning - comprises steel plate welded to copper@ hanger bar surface by nickel@- copper@ weld metal

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3589874A (en) * 1968-08-02 1971-06-29 Olin Corp Composite of copper base alloy on steel
US3830710A (en) * 1971-01-08 1974-08-20 Int Nickel Co Masked electrode structure and process for electrolytic deposition of metals
US3928152A (en) * 1974-02-25 1975-12-23 Kennecott Copper Corp Method for the electrolytic recovery of metal employing improved electrolyte convection

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4670124A (en) * 1985-08-31 1987-06-02 Norddeutsche Affinerie Aktiengesellschaft Cathode for use in the electrolytic refining of copper and method of making same
US4882027A (en) * 1986-02-06 1989-11-21 Kidd Creek Mines Ltd. Cathode hangers
EP0454056A1 (en) * 1990-04-23 1991-10-30 Austria Metall Aktiengesellschaft Aluminium cathode-plate for the electrowinning of zinc
WO2003031692A2 (en) * 2001-10-02 2003-04-17 Norddeutsche Affinerie Aktiengesellschaft Electrolysis cathode
WO2003031692A3 (en) * 2001-10-02 2003-08-14 Norddeutsche Affinerie Electrolysis cathode
EP1428910A1 (en) * 2002-12-13 2004-06-16 Paul Wurth S.A. Method For Converting An Electrorefinery And Device For Use Therein
CN103726076A (en) * 2005-03-09 2014-04-16 斯特拉塔昆士兰有限公司 Stainless steel electrolytic plate
WO2008099057A1 (en) * 2007-02-13 2008-08-21 Outotec Oyj Method of manufacturing a cathode plate, and a cathode plate
US8062498B2 (en) 2007-02-13 2011-11-22 Outotec Oyj Method of manufacturing a cathode plate, and a cathode plate
CN101611175B (en) * 2007-02-13 2012-04-25 奥图泰有限公司 Method of manufacturing a cathode plate, and a cathode plate
US8038855B2 (en) 2009-04-29 2011-10-18 Freeport-Mcmoran Corporation Anode structure for copper electrowinning
US8372254B2 (en) 2009-04-29 2013-02-12 Freeport-Mcmoran Corporation Anode structure for copper electrowinning

Also Published As

Publication number Publication date
BE881500A (en) 1980-05-30
DE3003927A1 (en) 1980-08-07
YU42960B (en) 1989-02-28
FI68430C (en) 1985-09-10
MX155943A (en) 1988-05-27
ZM1480A1 (en) 1981-05-21
SE8000607L (en) 1980-08-06
JPS5943996B2 (en) 1984-10-25
CA1150669A (en) 1983-07-26
AU506521B1 (en) 1980-01-10
GB2040311B (en) 1983-02-09
JPS55110788A (en) 1980-08-26
SU1344252A3 (en) 1987-10-07
PL123151B1 (en) 1982-09-30
FI68430B (en) 1985-05-31
ES488250A0 (en) 1981-02-16
ES8103198A1 (en) 1981-02-16
FI800337A (en) 1980-08-06
MY8400147A (en) 1984-12-31
YU24180A (en) 1983-02-28
PL221801A1 (en) 1980-10-20
SE445050B (en) 1986-05-26
DE3003927C2 (en) 1986-06-05
BR8000692A (en) 1980-10-14
ZA80341B (en) 1981-01-28
PH17223A (en) 1984-07-03

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PE20 Patent expired after termination of 20 years

Effective date: 20000121