CA1154719A - Method for controlling 'end effect' on anodes used for cathodic protection and other applications - Google Patents

Method for controlling 'end effect' on anodes used for cathodic protection and other applications

Info

Publication number
CA1154719A
CA1154719A CA000368658A CA368658A CA1154719A CA 1154719 A CA1154719 A CA 1154719A CA 000368658 A CA000368658 A CA 000368658A CA 368658 A CA368658 A CA 368658A CA 1154719 A CA1154719 A CA 1154719A
Authority
CA
Canada
Prior art keywords
anode
shield
cylindrical
adjacent
spaced away
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
Application number
CA000368658A
Other languages
French (fr)
Inventor
George Riedl
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.)
Rio Tinto Alcan International Ltd
Original Assignee
Alcan International Ltd Canada
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 Alcan International Ltd Canada filed Critical Alcan International Ltd Canada
Application granted granted Critical
Publication of CA1154719A publication Critical patent/CA1154719A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F13/00Inhibiting corrosion of metals by anodic or cathodic protection
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S204/00Chemistry: electrical and wave energy
    • Y10S204/07Current distribution within the bath

Abstract

A B S T R A C T

'Necking' of elongated cathodic protection anodes is obviated or reduced by means of a non-conductive shield placed around the periphery of the anode, but spaced away from the surface of the anode at the end at which it is connected to a conductor cable. The gap between the shield and the electrode surface is generally in the range of 15 - 30% of the radius of curvature of the electrode surface.
The shield may extend over, but be spaced away from, the end surface of the electrode also.

Description

~ 7~1~

"Method for controlling 'end effect' on anodes used for cathodic protection and other appllcatlons~' The present invention relates to improvements in the performance of anodes made of metal~, semi-conductors and non-metals.
An anode is an electrode at which oxidation occurs and/or is the electron-emitting electrode.
Depending on the application and anode material, the mass of the anode d~creases at various rates during its operation, thus affecting the perfc,rmance and the life of the anode.
Anodes can be used as sacrificial or impressed current anodes for cathodic protection and other industrial processe~. All such anodes, both of the sacrificial and of the impressed current type, used in liquid electrolytes are subject to consumption regardless of what material the anode is made from.
In both cathodic protection and plating processes the anode is in many instances completely immersed in the electrolyte and, consequently, the electrical conductor (cable for example) connecting the anode with the cathode,'directly or 'through ~he current supply unit, is also expo~ed to the electrolyte. The electrical conductor and the connection between the anode and the electrical conductor must be protected from the chemi~al and electrochemlcal effect~ of ~he electrolyte.

~1 54~7
-2-The present inventlon i~ p~rticularly, but not exclu~ively9 directed to anodes (graphite, lead-silver etc.) oper~ting in so~called impres~ed current cathodic protection ~ystems, where the protected structure is rendered cathodic by connection to one or more anodes through a D.~. power source, both the protect~d structure and the anode(s) being within a common electrolyte, such as sea water or soil.
The invention is also applicable to so-called sacrificial anodeQ (aluminlumJ magne~ium, zinc), in which the ob~ect to be protected, such as a ship hull or ~tationary steel structure, ~orm5 a cathode which is directly connected to the anode by an electric~l conductor. A sacrificial anode i8 one which has a ~5 higher corrosion ra~e than the met~l to which it is connected in the electrolyte in which both are located.
It is a common practice to make the connection between an impressed current anode and an insulated cable or other conductor inside the anode and to ~eal off the connection with an inert nonoconductive m~terial to prevent ingress of the electrolyte. The anode-cable connection may be loc~ted a fsw inches or a few feet away from on2 end o the anode. In some sacrificial anodes, a small diameter steel core provides the connect~on over ~he e~tire le~gth of the ano&eO M~ny processes use elong~ted anodes, usually cylindrical anodes, and ln most cases the cqble or other conductor usually enters the anode ~t one end. In cathodic ~54~19 protection~ for example, the anodes may be 3 in.
to 6 ln. in diameter and 30 in. ~o 80 in. long.
The elongated shape of the anode, which has some theoretical and practical ~ustlfications, create~
increased concentration and di~charge of current at both ends of the anode. The high current density at the ends causes accelerated loss of anode material at these locations due to chemical and/or electrochemical reactions, or due to spalling. The current density is at a maximum in the region of any sharp edge, such as at the ~unction between a flat end and a cylindrical side surface of an anode.
In general, on cylindrical anodes the aotivity of the 'end effect' will be lowest when the anode h~s a radius to length ratio equal to 1~1. As the ratio changes, the activity of the 'end effect' increases at the smaller site.
On cyl~ndricàl anodes the 'e~d effect' will not only occur at the physical ends of the anodes, but also at the edge of any insulating clrcumerential obstruction around the cyllindr~cal part of the anode.
For example, if a tightly fitting plastic ring is installed at the middle of~-the anode, ~he-single anode -will behave like two individual anodes. The 'end effect' will be visible at both edge~ of the plastic ring. The inten~ity of the 'end effect' will depend on the length of the plast~c ring.

~ 7 ~

The result of an intensive 'end effect' at the edge of any circumferential obst~uction on the surface of the anode is called 'necking'. iNeck~ng', once triggered, reduces the diameter of the anode within a narrow band with increasing speed. Thls is because the curvature o the surface iQ continuously diminishing as the material of the anode is removed and i~ accompanied by increR~ing current density which increases the rate of removal. The result of 'necking' is that the anode fails prematurely at thi~
poi~t~
The ob~ecti~e of the present invention ~ 8 to greatly reduce or eliminate the 'end effect' and the 'necking'. This can be achieved by installing a circumferenti~l insul~ting obstruction spaced at a small, but su~stantial, distance from the surface of the a~ode at the area or are~s where high current denslty .-occurs.
Because of the space between the circumferential 2~ obstruction and the anode, the curren~ density discharged from the surface of the anode dimini~hes gradually a~ the anode disappears inside of the obstruction. The reduction of current output i8 CAU~ed by the fact that the ~urf~ce of the anode is prevented from discharging in the direction of the cathode.
The shield may b~ cylindrical or bell-shaped, and ha~e any cros section required to correspo~d to the shape of ~he anode. It m~y be open or closed at ~ne end, ~ 71 ~

with or without openings for release of gases and/or for cirrula~ion of electrolyte. The ~pace between the anode ~urface and the shield i5 substantial although small in relation to the radlus of curvature of the adjacent surface of the anode. The space between the shleld and the anode is preferably somewhat proportionate to the diameter of a cylindrical anode. Conveniently it may be 0.3 cm~ for anodes of 2.5 cm. di~meter, 0.3 cm. to 1.0 cm. for anodes of 2.5 cm. to 10 cm. diameter and 1 cm. to 2.5 cm. for larger anodes. Thus it is preferred that the initial gap between the ~hield and the ad~cent 3urface of the anode ~8 15 - 30% of the r~diu~ of curvature of the ~node surface.
For elongated anodes having a length of at least 12 times the diameter and having ~n a~ode-cable connector installed in on~ end of ~he anode, the ~xl~l length of the shield should be Approximately equ~l to the diameter of the anode. In ~ny caset the ~ower end of the shield should be approximately 2.5 - 5 cmsO
below ~he upper end of the cylindrLcal Isurface of a vertically arranged anode.
On ~hort, st~bby anodes havin~g a relati~ely large diameter of 15 cmsO or more, the Length of the 2S shield may~be reduced-to approximately ,Dne quarter of the anode diameter. Where a connéctor i~ located within the anode it is preferred that the lower edge of the ~hield ~hould extend beyond the end of the 4~ g connector. It becomes of less importance to have an actual overlap as the diameter of the anode is increased beyond 15 cms.
The shield permits the anode-cable connector to be closer to the end of the anode and thus allows a more complete consumption of the anode.
Without the shield the increased consumption of the anode material at the end region frequently results in premature failure of the anode around the connector.
In many cathodic protection applications the use of the shield would not only control the 'end effect' and 'necking' but would also permit the in-stallation of the anode-cable connection close to the end of the anode. This would facilitate machining and assembly.
Thus, in accordance with one broad aspect of the invention, there is provided a method of improving the performance of a generally cylindrical anode located in contact with a corrosive medium which comprises placing a shield formed of electrically non-conducting material around a short length of the cylindrical surface of the anode at at least one end of said anode, said shield being spaced away from said cylindrical surface by a substantial dis-tance which is small in relation to the radius of curvature of said cylindrical surface.
In accordance with another broad aspect of the invention there is ?rovided an anode assembly comprising an elongated body of electrically con-ductive material, an insulated conductor electrically connected to said body internally thereof and extending substantially axially out of one end of said body, a cup-shaped non-conducting shield member having an end portion surround-ing said insulated conductor and spaced away from the adjacent surface of said body and a generally cylindrical wall portion extending around but spaced away from the adjacent peripheral surface of said elongated body at at least one end thereof, said end portion and said cylindrical wall portion being arranged to ~154~i9 permit unrestrained access of liquid to the surfaces of said body facing said end portion and said cylindrical wall portion, said body projecting beyond said cylindrical wall portion.
Referring to the accompanying drawing it will be seen that an im-pressed current anode consists of a solid cylinder 1 of anode material, such as graphite, lead-silver or aluminium. A metal connector 2 connects the anode to a conductor cable 3, the insulation 4 of the cable being embedded in sealant 5. The protector shield is in the form of a plastic moulding, having a shield holder 6, a cover 7 and a cylindrical shield 8. The shield is formed with vents 9 for escape of gas.
The interrupted lines on the anode indicate the approximate future shape of the anode on discharge of current.
Extensive laboratory tests in liquid electrolytes were conducted using graphite, aluminium 6a-- :

;~ 5~9 and magnesium anodes. The aluminium and magnesium anodes were operated either as sacrificial anodes or parallel with graphite as impressed current anodes at low and at very high current densities. In all modes of operation accelerated corrosion at the protected location was avoided and the service life of the anode was consequently extended.
Tests were conducted to prove that the shield will perform equally well on any size of anode. The tests confirmed the effectiveness and per-formance of the shield installed on all types of anodes but particularly on the impressed current anodes discharging large amount of current.

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Claims (10)

1. A method of improving the performance of a generally cylindrical anode located in contact with a corrosive medium which comprises placing a shield formed of electrically non-conducting material around a short length of the cylindrical surface of the anode at at least one end of said anode, said shield being spaced away from said cylindrical surface by a substantial distance which is small in relation to the radius of curvature of said cylindrical surface.
2. A method according to claim 1 in which the initial gap between the surface of the shield and the adjacent cylindrical surface of the anode is 15 - 30%
of the radius of curvature of the anode.
3. A method according to claim 1 further comprising placing a shield of electrically non-conducting material to face the end surface of said electrode adjacent said cylindrical surface, said shield being spaced away from said end surface to permit access of said corrosive medium thereto.
4. A method according to claim 3 further comprising providing at least one gas escape passage for release of gas generated within the gap between said shield and the adjacent cylindrical surface of the anode.
5. An anode assembly comprising an elongated body of electrically con-ductive material, an insulated conductor electrically connected to said body internally thereof and extending substantially axially out of one end of said body, a cup-shaped non-conducting shield member having an end portion surround-ing said insulated conductor and spaced away from the adjacent surface of said body and a generally cylindrical wall portion extending around but spaced away from the adjacent peripheral surface of said elongated body at at least one end thereof, said end portion and said cylindrical wall portion being arranged to permit unrestrained access of liquid to the surfaces of said body facing said end portion and said cylindrical wall portion, said body projecting beyond said cylindrical wall portion.
6. An anode assembly according to claim 5 wherein said end portion of said shield member is flat, facing the end surface of said body.
7. An anode assembly according to claim 6 in which one or more gas escape passages are provided in said cylindrical portion adjacent its junction with said flat end portion.
8. An anode assembly according to claim 5 in which the cylindrical portion of said shield member is spaced away from the adjacent surface of said body, for entrance of liquid therebetween, by a distance equal to 15-30 per cent of the radius of curvature of said surface.
9. An anode assembly according to claim 5 in which the cylindrical portion of said shield overlaps the peripheral wall of said body by a distance of about 2.5 - 5 cm.
10. An anode assembly according to claim 5 in which the conductor is connected to the elongated body by means of a connector located axially within said body, the axial length of said cylindrical portion of said shield being sufficient to completely surround said connector.
CA000368658A 1980-01-18 1981-01-16 Method for controlling 'end effect' on anodes used for cathodic protection and other applications Expired CA1154719A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8001783 1980-01-18
GB8001783 1980-01-18

Publications (1)

Publication Number Publication Date
CA1154719A true CA1154719A (en) 1983-10-04

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ID=10510736

Family Applications (1)

Application Number Title Priority Date Filing Date
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US (1) US4420382A (en)
CA (1) CA1154719A (en)

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US4773977A (en) * 1987-04-16 1988-09-27 A. O. Smith Corporation Anode mounting construction for a water heater
GB8809750D0 (en) * 1988-04-25 1988-06-02 Beckswift Ltd Electrical apparatus
US5290583A (en) * 1992-04-02 1994-03-01 David Reznik Method of electroheating liquid egg and product thereof
US5571550A (en) * 1993-01-22 1996-11-05 Polny, Jr.; Thaddeus J. Methods for electroheating food employing concentric electrodes
CA2132882A1 (en) * 1993-09-23 1995-03-24 David Reznik Electroheating of food products using low frequency current
US5583960A (en) * 1994-06-01 1996-12-10 David Reznik Electroheating apparatus and methods
US5741539A (en) * 1995-06-02 1998-04-21 Knipper; Aloysius J. Shelf-stable liquid egg
US5897755A (en) * 1997-01-31 1999-04-27 Carsonite International Corporation Cathodic protection test station
US5855747A (en) * 1997-04-04 1999-01-05 Aos Holding Company Performance enhancing coating for water heater
US6174425B1 (en) * 1997-05-14 2001-01-16 Motorola, Inc. Process for depositing a layer of material over a substrate
US6220200B1 (en) 1998-12-02 2001-04-24 Carsonite International Line marker with locking mechanism
US6231743B1 (en) 2000-01-03 2001-05-15 Motorola, Inc. Method for forming a semiconductor device
US8094784B2 (en) 2003-04-25 2012-01-10 Rapiscan Systems, Inc. X-ray sources
US9208988B2 (en) 2005-10-25 2015-12-08 Rapiscan Systems, Inc. Graphite backscattered electron shield for use in an X-ray tube
US10483077B2 (en) 2003-04-25 2019-11-19 Rapiscan Systems, Inc. X-ray sources having reduced electron scattering
US8243876B2 (en) 2003-04-25 2012-08-14 Rapiscan Systems, Inc. X-ray scanners
GB0812864D0 (en) 2008-07-15 2008-08-20 Cxr Ltd Coolign anode
US8331535B2 (en) * 2003-04-25 2012-12-11 Rapiscan Systems, Inc. Graphite backscattered electron shield for use in an X-ray tube
GB0525593D0 (en) 2005-12-16 2006-01-25 Cxr Ltd X-ray tomography inspection systems
US9046465B2 (en) 2011-02-24 2015-06-02 Rapiscan Systems, Inc. Optimization of the source firing pattern for X-ray scanning systems
GB0816823D0 (en) 2008-09-13 2008-10-22 Cxr Ltd X-ray tubes
GB0901338D0 (en) 2009-01-28 2009-03-11 Cxr Ltd X-Ray tube electron sources
WO2010141659A1 (en) * 2009-06-03 2010-12-09 Rapiscan Security Products, Inc. A graphite backscattered electron shield for use in an x-ray tube
KR200464956Y1 (en) 2010-10-22 2013-01-25 주식회사 우진 Cathodic protection anode for preventing separation of electric wire
GB201210929D0 (en) * 2012-06-20 2012-08-01 E M & I Maritime Ltd Apparatus and method
US10585206B2 (en) 2017-09-06 2020-03-10 Rapiscan Systems, Inc. Method and system for a multi-view scanner
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Also Published As

Publication number Publication date
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