[0001] This invention relates to corrosion protection using a sacrificial material.
BACKGROUND OF THE INVENTION
[0002] U.S. Patent 6,346,188 (Shuster) assigned to ENSER Corporation and issued February 12, 2002 discloses a method for
corrosion protection of marine piles in which an anode is located within a jacket
surrounding the pile at water level and a battery is mounted on the pile above the
water level for providing an impressed current between the anode of the jacket and
the steel of the pile. The anode is preferably formed of titanium or other non-corroding
materials which are high on the Noble scale. However the patent mentions that other
materials such as zinc can be used but these are disadvantageous since they tend to
corrode. The intention is that the battery have a long life and be maintained effectively
so that the impressed current remains in place during the life of the marine pile
bearing in mind that the salt water in the marine environment is particularly corrosive.
[0003] Such impressed current systems can use other types of power supply including common
rectifiers which rectify an AC voltage from a suitable source into a required DC voltage
for the impressed current between the anode and the steel. It is also known to provide
solar panels for charging batteries to be used in a system of this type.
[0004] In all cases such impressed current systems require regular maintenance and checking
of the status of the power supply to ensure that the power supply does not fail leading
to unexpected and unacceptable corrosion of the steel within the structure to be protected.
While such maintenance can be carried out and the power supply thus ensured, this
is a relatively expensive process.
[0005] Alternatively galvanic systems can be used which avoid necessity for any power supply
since the voltage between the steel and the anode is provided by selecting a suitable
material for the anode which is sufficiently electro-negative to ensure that a current
is generated to provide a corrosion protection. These systems have obtained considerable
success and are widely used.
[0006] There are two primary limitations of ordinary galvanic anodes as used in steel reinforced
concrete. The first relates to the mass of zinc per anode which, depending on the
required current output, limits the useful life of the anode. The second is the actual
current output of the anode which may or may not be sufficient to halt corrosion of
the steel. The current output is limited by the driving voltage, which is essentially
a fixed property and varies with exposure conditions, age of the anode, and build
up of corrosion products overtime.
SUMMARY OF THE INVENTION
[0007] It is one object of the invention to provide an improved method for corrosion protection.
[0008] According to one aspect of the invention there is provided a method for use in corrosion
protection of a metal section in an ionically conductive covering material comprising:
locating a sacrificial anode of a sacrificial material in ionic contact with the ionically
conductive material;
causing the sacrificial anode to corrode preferentially in relation to the metal section
such that ions of the sacrificial material are generated from the sacrificial anode,
thus depleting the sacrificial anode as the sacrificial anode corrodes;
and recharging the sacrificial anode with ions of the sacrificial anode material.
[0009] Preferably the sacrificial anode is re-charged by locating an impressed current anode
in ionic contact with the ionically conductive material and connecting a first terminal
of a DC power supply to the impressed current anode so as to cause ionic current to
flow through material to cause sacrificial anode ions to be deposited on the sacrificial
anode.
[0010] Preferably sacrificial anode ions are present in the ionically conductive material.
[0011] Preferably the re-charging causes hydroxyl ions to be generated at the surface of
the sacrificial anode.
[0012] Preferably the re-charging causes an alkali environment to be re-generated around
the sacrificial anode.
[0013] Preferably, in a first step, the sacrificial anode is connected to the metal section
to provide corrosion protection of the metal section by the corrosion of the sacrificial
anode which results in the formation of corrosion products of the sacrificial anode
and, in a second step after corrosion of the sacrificial anode has occurred, the current
supplied by a DC power supply causes the ions of the sacrificial material, from the
corrosion products of the sacrificial anode, to be re-deposited on the sacrificial
anode.
[0014] Preferably the DC power supply is applied temporarily.
[0015] Preferably there are ions of the sacrificial material available to be deposited.
[0016] Preferably the ions of the sacrificial material are soluble.
[0017] Preferably the ions of the sacrificial material are electrochemically mobile.
[0018] Preferably the metal section is steel and the ionically conductive material is concrete
or mortar.
[0019] According to a second aspect of the invention there is provided a method for use
in corrosion protection of a metal section in an ionically conductive covering material
comprising:
locating an impressed current anode in ionic contact with the ionically conductive
material;
locating a sacrificial anode in ionic contact with the ionically conductive material;
providing a DC power supply;
connecting a first terminal of a DC power supply to the impressed current anode;
connecting a second terminal of the DC power supply to the sacrificial anode so as
to cause ionic current to flow through material to cause sacrificial anode ions to
be deposited on the sacrificial anode.
[0020] Preferably there is provided a connection between the sacrificial anode and the metal
section so that the sacrificial anode provides corrosion protection.
[0021] Preferably the connection between the sacrificial anode and the metal section remains
in place when the DC power supply is in operation.
[0022] In one arrangement, at least a portion of the sacrificial anode is fabricated in
the ionically conductive material by depositing ions of the sacrificial material,
[0023] In this case the method can include incorporating ions of the sacrificial material
in the ionically conductive material where the sacrificial anode is generated in the
ionically conductive material by depositing the incorporated ions of the sacrificial
material on the sacrificial anode.
[0024] Preferably the second terminal of the DC power supply is connected to the sacrificial
anode and to the metal section.
[0025] Preferably the connection of the DC power supply across the impressed current anode
and the metal section creates a current between the metal section and the impressed
current anode which is used to passivate the metal section.
[0026] Preferably the connection of the DC power supply across the impressed current anode
and the metal section creates a current between the metal section and the impressed
current anode which is used to provide corrosion protection to the metal section while
the ions of the sacrificial material are being deposited on the sacrificial anode.
[0027] Preferably the sacrificial anode and the impressed current anode comprise common
components of an anode apparatus so that, when the common components of the anode
apparatus are located in the ionically conductive material, each of the sacrificial
anode and the impressed current anode is in ionically conductive communication with
the other and with the metal section.
[0028] Preferably the impressed current anode and the sacrificial anode are electrically
separated to prevent electrical communication therebetween.
[0029] Preferably the impressed current anode is perforated so to allow passage of ionic
current in the ionically conductive material to pass through the impressed current
anode.
[0030] Preferably the sacrificial anode forms a rod and the impressed current anode forms
a sleeve surrounding the rod.
[0031] Preferably the impressed current anode and the sacrificial anode comprise side by
side plates.
[0032] Preferably there is provided an ionically conductive filler material between the
impressed current anode and the sacrificial anode.
[0033] Preferably the ionically conductive filler material is different from the ionically
conductive material.
[0034] Preferably the ionically conductive filler material contains sacrificial anode ions
[0035] Preferably the ionically conductive filler material is porous.
[0036] Preferably the ionically conductive filler material is deformable.
[0037] Preferably the ionically conductive filler material contains at least one activator
to ensure continued corrosion of the sacrificial anode.
[0038] Preferably the ionically conductive filler material is hydroscopic.
[0039] Preferably the ionically conductive filler material has a pH sufficiently high for
corrosion of the sacrificial anode to occur and for passive film formation on the
sacrificial anode to be avoided.
[0040] Preferably there is provided a plurality of sacrificial anodes and wherein the impressed
current anode is separate from said sacrificial anodes.
[0041] Preferably there is provided a plurality of impressed current anodes and wherein
the sacrificial anode is separate from said impressed current anodes.
[0042] Preferably the impressed current anode is arranged to be mounted temporarily to provide
current through a surface of the ionically conductive material.
[0043] Preferably there are sacrificial anode ions available to be deposited.
[0044] Preferably the sacrificial anode ions are soluble.
[0045] Preferably the sacrificial anode ions are electrochemically mobile.
[0046] Although not essential, typically this arrangement is designed for use where the
metal section is steel and the ionically conductive material is concrete or mortar.
[0047] In some cases a portion of the structure or the sacrificial anode is wetted.
[0048] In some cases the impressed current anode is mounted temporarily for the purpose
of causing the ions of the sacrificial material to be deposited.
[0049] The above methods can be carried out using an anode apparatus for cathodically protecting
a metal section in an ionically conductive material, the anode apparatus comprising:
a sacrificial anode of a material which is less noble than the metal section;
an impressed current anode;
the sacrificial anode and the impressed current anode comprising components of the
anode apparatus so that, when the components of the anode apparatus are located in
contact with the ionically conductive material, each of the sacrificial anode and
the impressed current anode is in ionically conductive communication with the other
and with the metal section;
the impressed current anode and the sacrificial anode being electrically separated
to prevent electrical communication therebetween;
a first electrical connector arranged for connection to the sacrificial anode;
and a second electrical connector arranged for connection to the impressed current
anode.
[0050] This anode apparatus can be used in a method for corrosion protection of a metal
section in an ionically conductive covering material where the impressed current anode
and the sacrificial anode are both located in contact with the ionically conductive
material and a DC power supply is connected between the impressed current anode and
the metal section so as to create a current between the metal section and the impressed
current anode which is used to passivate the metal section and, while the first step
is terminated, there is a connection between the sacrificial anode and the metal section
so that the sacrificial anode continues to provide corrosion protection.
[0051] Preferably this is used where, in a first step, the sacrificial anode is connected
to the metal section to provide corrosion protection of the metal section by corrosion
of the sacrificial anode which generates corrosion products of the sacrificial anode
material in the ionically conductive material and wherein, in a second step after
corrosion of the sacrificial anode has occurred, the current applied by the DC power
supply through the ionically conductive material causes the sacrificial anode ions,
from the corrosion products of the sacrificial anode material, to be re-deposited
on the sacrificial anode. In a similar manner, sacrificial anode ions may be deposited
to create a sacrificial anode or to increase the size of an existing sacrificial anode.
[0052] In this method the recharging or deposition process can be used repeatedly and periodically
to ensure continued operation of the anode apparatus over a much longer period than
would be possible with the given quantity of the zinc or other galvanic material such
as aluminum, magnesium or other material (which is less noble than the metal section
to be protected) in the anode. This can be done, for example, using a solar cell where
the re-charging occurs each day. Alternatively and more typically, this is done by
periodic maintenance where a worker visits the site periodically and applies a power
supply for a period of time necessary to effect the re-charging.
[0053] In one particular aspect of the invention, which is independently patentable, there
is provided an apparatus for cathodically protecting a metal section in an ionically
conductive material comprising an impressed current anode and a conductor which can
eventually form a sacrificial anode where the sacrificial anode and the impressed
current anode comprising components of the anode apparatus so that, when the components
of the anode apparatus are located in contact with the ionically conductive material,
each of the sacrificial anode and the impressed current anode is in ionically conductive
communication with the other and with the metal section. In this way the above described
charging of the sacrificial anode can take place wholly in situ so that the ions are
applied onto the conductor by deposition from the ionically conductive material. As
set out above, the impressed current anode and the sacrificial anode should be electrically
separated to prevent electrical communication therebetween
[0054] In one arrangement, to provide the ions, the impressed current anode can be formed
of the sacrificial anode material such as zinc so that application of the DC power
causes corrosion of the impressed current anode and generates sacrificial anode ions
which are then available to be deposited on the sacrificial anode. However the ions
of the sacrificial material can be provided in the ionically conductive material itself
or in an additional filler material at or adjacent the sacrificial anode.
[0055] Preferably, simultaneously with the connecting of the second terminal of the DC power
supply to the sacrificial anode, the second terminal of the DC power supply is also
connected to the metal section such that the first terminal of the power supply is
connected to the impressed current anode and the second terminal of the power supply
is connected to the sacrificial anode and the metal section. This arrangement can
be used not only to cause the recharging action but also acts to provide enhanced
protection of the metal section by generating a protective current which may be greater
than the galvanic current alone to effect passivation of the steel (metal section)
while providing the option of re-charging the sacrificial anode at the same time.
[0056] Connecting the sacrificial anode to the metal section can provide a galvanic corrosion
protection back up to provide corrosion protection to the metal section when the DC
power supply or impressed current anode system is not functional. Having the sacrificial
anode connected to the metal section provides a simple, automatic corrosion protection
back up system should the impressed current system become non-operational.
[0057] The term impressed current anode used herein is intended to distinguish from the
sacrificial anode where the sacrificial anode is formed of a material, typically of
zinc, which is less noble than the metal section so that it preferentially corrodes
relative to the metal section to be protected. The impressed current anode is one
which is used in conjunction with an external power supply and does not need to be
less noble than the metal section. Typically such impressed current anodes are formed
of titanium, carbon and other noble metals and oxides which do not corrode readily,
or they can be formed of steel or less noble materials such as zinc.
[0058] The sacrificial anode and the impressed current anode preferably form common components
of the anode apparatus. That is, the apparatus as supplied for use includes both components
as a common system. However they may or may not be assembled into a common attached
construction which can be inserted into the material or applied onto the surface as
a common assembly. A common assembly is, of course, preferred for convenience but
the components can be inserted separately, for example, in one or in separate drilled
holes or slots in a concrete construction, installed in new concrete or applied separately
to the concrete surface or elsewhere. The impressed current anode for example can
be applied temporarily to the outer surface of the ionically conductive material such
as a plate attached to the exterior surface of the concrete for recharging sacrificial
anodes within the body of the concrete.
[0059] The apparatus preferably includes as a part of the apparatus a DC power supply with
positive and negative terminals. This can be any form of device which can provide
a DC output at a required voltage such as a battery, solar cell or it can be a rectifier.
The power supply may also be supplied separately and/or temporarily so that it is
not itself an integral component of the apparatus. However in the method of use of
the system a suitable source of DC power must be used at least during a part of the
time.
[0060] As a further component of the apparatus, there is preferably provided a switchable
junction box having connectors for connection to the positive and negative terminals
of the power supply, to the first and second electrical connectors and to the metal
section. This can, however, be provided as separate components, again not an integral
part of the system. Also connections can be made on site without a specific switchable
junction box.
[0061] Preferably the impressed current anode is perforated so to allow passage of ionic
current to pass through the impressed current anode. However this is not essential
since the impressed current anode and the sacrificial anode can comprise separate
elements merely located in adjacent relationship for cooperation in the material.
The ionic current must pass from the sacrificial anode to the metal section but this
can pass through or around the impressed current anode or around parts of the impressed
current anode. However, where the sacrificial anode and the impressed current anode
are formed as a common assembly, it is preferred that the ionic current passes through
or around the impressed current anode. The impressed current anode may therefore be
formed as separate pieces or spaced apart to allow current to pass to the metal section.
Thus for example the impressed current anode can be perforated by macroscopic holes
formed through or cut into the anode.
[0062] In another preferred example, the impressed current anode is formed from electrically
conductive components in a matrix and there are provided spaces in the matrix between
the conductive components to allow the ionic current to pass through the matrix. This
can be achieved, for example, by sintering the anode material and / or other materials
or reducing oxides to form an electrically conductive matrix.
[0063] In order to obtain uniform, symmetrical deposition of the anode material on the sacrificial
anode during recharging, when that process is being used, it is preferred that the
impressed current anode surrounds the sacrificial anode, that is the impressed current
anode is arranged in a plane containing the sacrificial anode to fully, substantially
fully, partially, or discretely surround the sacrificial anode so that ionic current
passing to or from the sacrificial anode around 360 degrees in the plane passes through
the impressed current anode. If the impressed current anode is arranged wholly or
partly to one side, the deposition will occur preferentially to that side and hence
may be less effectively deposited. Therefore preferably, in a coaxial arrangement,
the sacrificial anode forms a rod and the impressed current anode forms a sleeve surrounding
the rod. Alternatively, the sacrificial anode may be in the form of a plate or rod
or ribbon or other similar element and the impressed current anode may be placed on
one side of the plate such that the deposition may occur primarily on the one side
of the sacrificial anode to which the impressed current anode is placed.
[0064] Preferably there is provided an ionically conductive filler material which is not
the ionically conductive material itself which is located between the impressed current
anode and the sacrificial anode and thus preferably in the coaxial arrangement, the
filler material forms a cylinder surrounding the rod. Preferably, the ionically conductive
filler material is in ionic contact with at least part of the surface of the sacrificial
anode.
[0065] For use during a sacrificial or galvanic phase of operation of the above method,
the ionically conductive filler material preferably contains at least one activator
to ensure continued corrosion of the sacrificial anode. However the activator can
also be located at other positions in the system. Suitable filler materials can be
in the form of solids, gels or liquids. Suitable activators include alkali hydroxides,
humectants, catalytic materials and other materials which are corrosive to the sacrificial
anode metal. Activators may be used alone or in combination.
[0066] For use during a sacrificial or galvanic phase of operation of the above method,
the ionically conductive filler material preferably has a pH sufficiently high for
corrosion of the sacrificial anode to occur and for passive film formation on the
sacrificial anode to be avoided. Alternatively, the filler may have a lower pH and
/ or contain activators for corrosion of the sacrificial anode to occur and for passive
film formation on the sacrificial anode to be avoided.
[0067] The anode and methods herein are preferably designed for use where the metal section
is steel and the ionically conductive material is concrete or mortar.
[0068] The anode apparatus including the impressed current and sacrificial components is
typically buried in the concrete or other solid material so that it is fully encased
by the concrete, but this is not essential and the anode may be only partially buried
or in physical or ionic contact with the concrete.
[0069] The anode apparatus including the impressed current and sacrificial components may
be surrounded by an encapsulating material or ionically conducting filler material
which may be a porous material or porous mortar material. Suitable encapsulating materials
can be inorganic or organic and may be any cementitious, polymer or non-cementitious
material or mortar including geopolymers or modified portland cements. The encapsulating
material may be solid, gel or liquid and may be deformable.
[0070] The intention is therefore, in the arrangement described in more detail hereinafter,
to marry a galvanic anode with an impressed current anode for use with an impressed
current and/or re-chargeable galvanic anode system. The configuration allows the impressed
current anode to deliver current either to the steel reinforcement or the galvanic
anode separately, or to both the steel reinforcement and the galvanic anode concurrently.
The anode assembly can be used in three different ways, that is, a) as a normal galvanic
anode, b) as an impressed current anode, and c) importantly, as a rechargeable galvanic
anode. The assembly preferably includes an inner zinc core acting as the galvanic
anode, surrounded by a suitable activating electrolyte. The zinc and activator are
preferably encased within a porous or mesh-type impressed current electrode.
[0071] The galvanic anode provided herein can therefore be flexible in operation so that
continuous protection can be provided to a structure or structural component over
periods compatible with impressed current corrosion protection systems.
[0072] The configuration can allow the impressed current anode to deliver cathodic current
either to the steel reinforcement, to the galvanic anode or to the steel reinforcement
and galvanic anode together. The anode assembly is to be used in three different ways,
viz., as a normal galvanic anode, as an impressed current anode and most importantly,
as a rechargeable galvanic anode. The latter capability allows multiple use of the
same mass of zinc as it is recycled into the activating electrolyte and back from
the electrolyte in the recharging process, eliminating the need for the use of larger
volume anodes for long term protection.
[0073] In a preferred arrangement in an alkaline activator, the corrosion product of zinc
is ultimately believed to be primarily zinc oxide. It is possible, therefore, to reverse
the corrosion process and redeposit zinc metal back into the anode assembly. The arrangement
described herein provides a method of re-depositing zinc metal without having to remove
the anode assembly from the structure it is protecting. A counter or impressed current
electrode which can be used as an anode for re-charging the zinc is provided. This
counter electrode is preferably part of the anode assembly. The same electrode can
then be utilised if there is a need to change the setup into an impressed current
system.
[0074] The sacrificial anode may be any of the more electro-negative materials such as zinc,
aluminum, magnesium or alloys thereof.
[0075] The DC power supply can be a battery. The power supply may be a rectifier generating
DC power from an AC supply voltage. Preferably the DC power supply has a potential
greater than 1.5V. Where the power supply is a battery it can be rechargeable. Where
the power supply is a battery it can be replaceable in the assembly. This is a convenient
way periodically to do the recharge and/or provide an additional step of the impressed
current to the steel by inserting a new battery and just leaving it until it becomes
depleted, whereupon and the system then works galvanically until a later time when
the depleted battery is removed and another one is inserted. The battery can be mounted
at any convenient location, such as in the junction box or monitoring unit or somewhere
convenient. A single battery can supply power to a group of anodes.
[0076] The power supply may include a solar panel which drives the impressed current anode
and rechargeable galvanic anode so as to provide long term protection when the solar
power is on and off.
[0077] According to another aspect of the invention there is provided a method for corrosion
protection of a metal section in an ionically conductive covering material comprising:
locating an impressed current anode in contact with the ionically conductive material;
locating a sacrificial anode of a material which is less noble than the metal section
in contact with the ionically conductive material;
providing a DC power supply;
providing a connection of the DC power supply across the impressed current anode and
the metal section so as to create a current between the metal section and the impressed
current anode to provide corrosion protection of the metal section;
and providing a connection between the sacrificial anode and the metal section so
that the sacrificial anode to provide corrosion protection of the metal section.
[0078] The connection across the impressed current anode and the connection to the sacrificial
anode can be in place simultaneously or either can be connected when required. The
connection of either can be carried out manually using simple connectors or using
a switch box or by an automatic control system.
[0079] In one arrangement of the above method, the connection of the DC power supply across
the impressed current anode provides an initial impressed current and, when the initial
impressed current is terminated, the connection between the sacrificial anode and
the metal section continues to provide corrosion protection.
[0080] In another arrangement of the above method, the connection between the sacrificial
anode and the metal section provides corrosion protection and, subsequent to a period
of the corrosion protection provided by the sacrificial anode, the DC power supply
is connected across the impressed current anode causing the metal section to be further
protected. This can be carried out periodically during the operation of the sacrificial
anode. After initial installation, the first action in protection can be either the
sacrificial anode or the impressed current anode as selected by the person skilled
in the art in accordance with the status of the installation.
[0081] In both cases, the connection of the sacrificial anode can be in place while the
impressed current is in connected or can be connected when the impressed current is
terminated.
[0082] Preferably the initial current provided by the impressed current anode is sufficient
to passivate the metal section. However the specific effect obtained in the first
step is not essential and other effects can be obtained advantageously using this
method.
[0083] Preferably the sacrificial anode and the impressed current anode comprise common
components of the anode apparatus so that, when the common components of the anode
apparatus are located in the ionically conductive material, each of the sacrificial
anode and the impressed current anode is in ionically conductive communication with
the other and with the metal section. However separate anode elements can be provided.
[0084] Preferably the impressed current anode and the sacrificial anode are electrically
separated to prevent electrical communication therebetween.
[0085] Preferably there are provided connectors for connection to the positive and negative
terminals of the power supply, with a first electrical connector connected to the
impressed current anode, with a second electrical connector connected to the sacrificial
anode and/or to the metal section.
[0086] Preferably the impressed current anode is perforated so to allow passage of ionic
current in the ionically conductive material to pass through the impressed current
anode. Many different techniques can be provided to obtain the effect of the perforation
so that the ionic current can pass through.
[0087] Preferably the sacrificial anode forms a rod and the impressed current anode forms
a sleeve surrounding the rod. However other arrangements can be provided such as parallel
or side by side plates.
[0088] Preferably there is provided an ionically conductive filler material adjacent to
the sacrificial anode where the ionically conductive filler material is different
from said ionically conductive material.
[0089] Preferably the ionically conductive filler material contains at least one activator
to ensure continued corrosion of the sacrificial anode. Many different types of activator
are available and can be used.
[0090] Preferably the ionically conductive filler material has a pH sufficiently high for
corrosion of the sacrificial anode to occur and for passive film formation on the
sacrificial anode to be avoided.
[0091] In one example there is provided a plurality of separate sacrificial anodes and the
impressed current anode is separate from said sacrificial anodes.
[0092] In another example there is provided a plurality of impressed current anodes and
wherein the sacrificial anode is separate from said impressed current anodes. However,
typically the sacrificial anode and the impressed current anodes are parts of a common
construction.
[0093] In another arrangement which can be used, the impressed current anode is mounted
temporarily to provide current through a surface of the ionically conductive material.
That is the impressed current anode is arranged to be mounted (utilized/ installed
and operated) temporarily during charging of the sacrificial anode.
[0094] The construction and methods proposed herein are designed particularly where the
metal section is steel and the ionically conductive material is concrete or mortar.
However the same arrangements may be used in other corrosion protection systems such
as for pipes or other constructions in soil, and in many other systems where such
anodes can be used.
[0095] Preferably there is provided a porous or deformable material to absorb corrosion
products from the sacrificial anode. This may be an encapsulating component or may
be in the sacrificial anode itself.
[0096] Preferably the assembly includes a reinforcing layer, such as disclosed in
US Patent 7,226,532 issued June 5 2007 to Whitmore, to which reference may be made for further detail, to restrain and resist forces
such as expansion, contraction and deformation forces which may be caused by corrosion
of the anodes, deposition of sacrificial anode ions and other physical / environmental
forces such as freezing, thawing, wetting, drying and thermal expansion / contraction.
[0097] The subject matter of the invention may also be described with reference to the following
clauses:
- 1. A method for corrosion protection of a metal section in an ionically conductive
covering material comprising:
locating an impressed current anode in ionic contact with the ionically conductive
material;
locating a sacrificial anode of a material which is less noble than the metal section
in ionic contact with the ionically conductive material;
providing a DC power supply;
providing a connection of the DC power supply across the impressed current anode and
the metal section so as to create a current between the metal section and the impressed
current anode to provide corrosion protection of the metal section;
and providing a connection between the sacrificial anode and the metal section so
that the sacrificial anode acts to provide corrosion protection of the metal section.
- 2. The method according to clause 1 wherein the application of the DC power supply
between the impressed current anode and the metal section provides an initial impressed
current and, when the initial impressed current is terminated, the connection of the
sacrificial anode and the metal section provides corrosion protection of the metal
section.
- 3. The method according to clause 1 wherein corrosion protection of the metal section
is provided by connection of the sacrificial anode and the metal section and, subsequent
to a period of corrosion protection provided by the sacrificial anode, the DC power
supply is applied between the impressed current anode and the metal section causing
the metal section to be further protected.
- 4. The method according to any one of clauses 1 to 3 wherein sacrificial anode remains
connected to the metal section during the impressed current.
- 5. The method according to any one of clauses 1 to 4 including passivating the metal
section by the impressed current.
- 6. The method according to any one of clauses 1 to 5 wherein the current provided
by the impressed current anode is applied until a minimum total charge of 20,000 Coulombs
per square meter is applied to the metal section.
- 7. The method according to any one of clauses 1 to 5 including charging the sacrificial
anode with sacrificial anode material from ions of the sacrificial anode material.
- 8. A method for use in corrosion protection of a metal section in an ionically conductive
covering material in which a sacrificial anode in ionic contact with the ionically
conductive material is caused to corrode preferentially in relation to the metal section
such that ions of the sacrificial material are depleted from the sacrificial anode
as the sacrificial anode corrodes;
characterized in the step of charging the sacrificial anode with sacrificial anode
material from ions of the sacrificial anode material.
- 9. The method according to clause 7 or 8 wherein the sacrificial anode is charged
by locating an impressed current anode in ionic contact with the sacrificial anode
and connecting a DC power supply to the impressed current anode so as to cause sacrificial
anode ions to be deposited on the sacrificial anode.
- 10. The method according to clause 9 wherein the impressed current anode is formed
of sacrificial anode material and application of a DC power causes corrosion of the
impressed current anode and generates sacrificial anode ions to be deposited on the
sacrificial anode.
- 11. The method according to any one of clauses 1 to 10 wherein the impressed current
anode is mounted in or on the covering material temporarily.
- 12. The method according to any one of clauses 7 to 11 wherein said ions of the sacrificial
material are provided for charging from the sacrificial anode, from material surrounding
the sacrificial anode or from the ionically conductive material.
- 13. The method according to any one of clauses 1 to 12 wherein, in a first step, the
sacrificial anode is connected to the metal section to provide corrosion protection
of the metal section by the corrosion of the sacrificial anode which results in the
formation of corrosion products of the sacrificial anode and wherein, in a second
step after corrosion of the sacrificial anode has occurred, current supplied by a
DC power supply causes the ions of the sacrificial material, from the corrosion products
of the sacrificial anode, to be re-deposited on the sacrificial anode.
- 14. The method according to any one of clauses 1 to 13 wherein the DC power supply
is connected to the impressed current anode and to the metal section and the sacrificial
anode wherein the metal section is protected and simultaneously the sacrificial anode
is charged with ions of the sacrificial material.
- 15. The method according to any one of clauses 1 to 14 including incorporating ions
of the sacrificial material in the ionically conductive material or in material adjacent
the sacrificial anode where the sacrificial anode is generated or fabricated in the
ionically conductive material by depositing the incorporated ions of the sacrificial
material on the sacrificial anode.
- 16. The method according to any one of clauses 1 to 15 wherein the DC power supply
is applied temporarily.
- 17. The method according to any one of clauses 1 to 16 wherein the DC power supply
is applied by a photovoltaic cell or by periodically replacing a battery.
- 18. An anode apparatus for cathodically protecting a metal section in an ionically
conductive material, the anode apparatus comprising:
a sacrificial anode of a material which is less noble than the metal section;
an impressed current anode;
the sacrificial anode and the impressed current anode comprising components of the
anode apparatus so that, when the components of the anode apparatus are located in
contact with the ionically conductive material, each of the sacrificial anode and
the impressed current anode is in ionically conductive communication with the other
and with the metal section;
the impressed current anode and the sacrificial anode being electrically separated
to prevent electrical communication therebetween;
an electrical connection to the sacrificial anode;
and an electrical connection to the impressed current anode.
- 19. The anode apparatus according to clause 18 including a DC power supply.
- 20. The anode apparatus according to clause 18 or 19 wherein the DC power supply comprises
a photovoltaic cell or battery.
- 21. The anode apparatus according to any one of clauses 18 to 20 wherein the impressed
current anode is perforated so to allow passage of ionic current to pass through the
impressed current anode.
- 22. The anode apparatus according to any one of clauses 19 to 21 wherein the impressed
current anode surrounds at least a portion of the sacrificial anode.
- 23. The anode apparatus according to any one of clauses 19 to 21 wherein the impressed
current anode and the sacrificial anode comprise side by side elements.
- 24. The anode apparatus according to any one of clauses 19 to 23 wherein there is
provided an ionically conductive filler material adjacent to the sacrificial anode.
- 25. The anode apparatus according to any one of clauses 19 to 24 wherein the anode
apparatus is provided as a preassembled assembly.
BRIEF DESCRIPTION OF THE DRAWINGS
[0098] One embodiment of the invention will now be described in conjunction with the accompanying
drawings in which:
Figure 1 is a schematic illustration of a corrosion protection method according to
the present invention using a first arrangement of anode apparatus.
Figure 2 is the schematic illustration of Figure 1 showing the connection of the components
for operation in the sacrificial protection mode.
Figure 3 is the schematic illustration of Figure 1 showing the connection of the components
for operation in the impressed current protection mode.
Figure 4 is the schematic illustration of Figure 1 showing the connection of the components
for operation in the re-charging mode.
Figure 5 is the schematic illustration of Figure 1 showing the connection of the components
for operation in the combined recharging and impressed current modes.
Figure 6 is a schematic illustration of a corrosion protection method according to
the present invention using a second arrangement of anode apparatus.
Figure 7 is a schematic illustration of a further corrosion protection method according
to the present invention using a further arrangement of anode apparatus where an existing
sacrificial anode is re-charged by a temporary plate electrode mounted on an exterior
surface of the concrete ionically conductive material.
Figure 8 is a cross-sectional view through a first example of an anode apparatus according
to the invention.
Figure 9 is a graph of current output of the anode of Figure 8 to steel, a) with the
anode as originally made, b) with the anode after a period of charging via the porous
conductive impressed current anode.
Figure 10 is a graph of cumulative charge output of the anode of Figure 8 to steel,
a) with anode as originally made, b) after a period of charging via the porous conductive
tube.
Figure 11 is a cross-sectional view of a second example of an apparatus according
to the present invention.
Figure 12 is a plan view of a test arrangement for the embodiment of Figure 11.
[0099] In the drawings, like characters of reference indicate corresponding parts in the
different figures.
DETAILED DESCRIPTION
[0100] In Figure 1 is shown a covering material 10 within which is embedded steel material
11 and an anode body 12.
[0101] The covering material 10 is a suitable material which allows communication of ions
through the covering material between the anode body 12 and the steel 11. The covering
material is generally concrete but can also include mortar or masonry materials, or
soil, water or other ionically conductive material, where there is a steel structure
which requires corrosion protection to prevent or inhibit corrosion. The steel material
11 is illustrated as being a reinforcing bar arrangement but other steel elements
can be protected in the manner of the arrangement shown herein including steel structural
members such as lintels, steel beams and columns, pipes, tanks or other elements in
contact with the concrete or other covering material.
[0102] The anode member may include or be constructed in part as the arrangement shown in
US Patents 6,027,633 issued Feb. 22, 2000;
6,165,346 issued Dec. 26, 2000;
6,572,760 issued June 3, 2003 6,793,800 issued Sept. 21, 2004,
7,226, 532 issued Jun 5, 2007,
7,914,661 issued Mar 29, 2011, and
7,959,786 issued Jun 14, 2011 of the present inventor, and in
6,022,469 (Page) issued Feb. 8, 2000 and
6,303,017 (Page and Sergi) issued Oct 16, 2001 assigned to Vector Corrosion Technologies and in
6,193,857 (Davison) issued Feb. 27, 2001 assigned to Vector Corrosion Tech.,
Bennett 6,217,742 issued April 17, 2001,
7,160,433 issued Jan 9, 2007,
8,157,983 issued Apr 17, 2012 and
6,471,851 issued Oct 29, 2002 assigned to Vector Corrosion Technologies,
Giorgini 7,998,321 issued Aug 16, 2011,
Schwarz 7,851,022 issued Dec 14, 2010,
Glass et al. 8,211,289 issued July 3, 2012,
8,002,964 issued Aug 23, 2011,
7,749, 362 issued Jul 6, 2010,
7,909,982 issued Mar 22, 2011, and
7,704,372 issued Apr 27, 2010 assigned to Vector Corrosion Technologies, to which reference should be made for
further details as required.
[0103] A DC power supply 14 is provided which generates a voltage at terminals 15 and 16
of the power supply.
[0104] In the embodiment shown the power supply is formed by a battery which may be a lead
acid battery with an output of 6 or 12 volts and a lifetime of 1 to 20 weeks, or may
be a zinc air battery well known and commercially available which provides an output
voltage of the order of 1.5 volts and has a lifetime of the order of 3 to 5 years.
The voltage may drop during current draw in operation from the nominal value of 1.5
volts to as low as I.0 volts. Such batteries of this type are commercially available
from ENSER Corporation or others. A suitable battery may have a capacity up to 1200
ampere hours.
[0105] Alternative power supplies may be used including solar panels and conventional rectifiers
which require an exterior AC supply voltage and which convert the AC supply into a
DC voltage at the terminals 15 and 16.
[0106] The anode apparatus 12 includes a sacrificial anode 20 of zinc or other material
which is less noble than the metal section together with an impressed current anode
21. The sacrificial anode 20 is in the form of a rod and the impressed current anode
21 is in the form of a sleeve surrounding the rod with an ionically conductive filler
material 22 which is generally not the ionically conductive material 10 located as
a cylinder between the impressed current anode 21 and the sacrificial anode 20. In
this coaxial and combined structure, the impressed current anode is arranged in a
radial plane of a central axis of the rod to fully surround the circumference of the
sacrificial anode so that ionic current passing to or from the sacrificial anode around
360 degrees in the plane generally passes through the impressed current anode on its
path to the steel 11.
[0107] Thus the sacrificial anode 20 and the impressed current anode 21 form common components
of the anode apparatus 12 so that each of the sacrificial anode 20 and the impressed
current anode 21 is in ionically conductive communication with the other and with
the metal section. The filler material is not electrically conductive so that the
impressed current anode and the sacrificial anode are electrically separated to prevent
electrical communication therebetween.
[0108] A switchable junction box 23 is provided having connectors 231 and 232 for connection
to the positive and negative terminals of the power supply. The box further includes
a connector 233 to a lead 236 to the impressed current anode 21, a connector 234 to
a lead 237 to the sacrificial anode 20 and a connector 235 to a lead 238 to the metal
section 11. Leads 236, 237 and 238 are preferably wires and are preferably corrosion
resistant. Lead 236 has the greatest need for corrosion resistance as it is connected
to an impressed current anode during operation. Examples of corrosion resistant materials
for the impressed current connection include titanium, niobium, nickel, platinized
wires and insulated wires.
[0109] The impressed current anode is perforated either with macroscopic holes 211 or a
microscopic structure so to allow passage of ionic current from the anode 20 to pass
through the impressed current anode. Macroscopic holes can be provided by forming
the impressed current anode in separate pieces.
[0110] In the arrangement where the anode 21 is perforated microscopically, the impressed
current anode has sufficient porosity and ionically conductive material within the
spaces between the impressed current anode material to allow the ionic current to
pass through the impressed current anode.
[0111] The ionically conductive filler material 22 preferably contains at least one activator
to ensure continued corrosion of the sacrificial anode. The ionically conductive filler
material preferably has a pH sufficiently high for corrosion of the sacrificial anode
to occur and for passive film formation on the sacrificial anode to be avoided or
minimized. For zinc, this pH is typically greater than 12 and may be greater than
13, 13.3 or 13.4. It is preferable that the zinc corrosion products remain partially
or substantially soluble. This can be achieved by incorporating ions or other chemicals
which are corrosive to the sacrificial anode material and/or prevent the surface of
the sacrificial anode material from passivating. Examples of materials which help
to produce soluble corrosion products and / or prevent passivation are disclosed in
the patent documents referenced above.
[0112] The ionically conductive filler material 22 is also preferably highly ionically conductive,
hygroscopic, and will accommodate volume changes as the sacrificial anode is charged
and discharged. The ionically conductive filler material may also be porous or deformable
to accommodate these changes.
[0113] In Figure 6 is shown a schematic illustration of the method using a second arrangement
of anode apparatus in which the sacrificial anode 20A and the impressed current anode
21A are formed as two parallel plates, mesh, ribbon or wires with the filler material
22A therebetween. In this case the re-charging of the sacrificial anode may occur
primarily on one side. In an alternative construction, the two parallel layers of
plates or mesh may be applied to the surface of the covering material.
[0114] In Figure 7 is shown a schematic illustration of the method using a further arrangement
of where an existing sacrificial anode 40 is re-charged by a temporary surface applied
electrode (impressed current anode) 41 on an exterior surface of the concrete 10 forming
the ionically conductive material. In this case a conductor 42 connects the impressed
current anode 41 to one terminal of the power supply 14 and a conductor 43 connects
the buried sacrificial anode 40 to the other terminal of the DC power supply. At the
same time the second terminal can be connected to the steel if the protection of the
steel is intended to continue during the re-charging process. Although the surface
applied electrode is a preferred embodiment for recharging an existing sacrificial
anode, other impressed current anodes such as embedded impressed current anodes may
be used.
[0115] The four separate functions provided by the junction box can be performed simply
as follows. These functions may also be performed manually by direct connection of
the appropriate connectors without the need for a junction box.
- a) Normal galvanic anode as shown in Figure 2: the zinc core is connected to the steel
via the junction box. The impressed current anode is set at the off position. This
allows the anode to perform as a simple galvanic anode.
- b) Impressed current anode as shown in Figure 3: the zinc anode is set to the off
position and the impressed current anode is connected to the steel via the DC power
source. The current output can be regulated by controlling the applied voltage.
- c) Recharging of galvanic anode as shown in Figure 4: the impressed current anode
is connected via the DC power source to the zinc anode. The steel is set to the off
position. This allows the zinc ions or zinc corrosion products present in the electrolyte
to be deposited onto the zinc core as zinc metal building up the thickness of the
zinc anode. Zinc oxide and zinc hydroxide are two common corrosion products produced
while the zinc anode is in operation.
- d) Recharging of galvanic anode and impressed current as shown in Figure 5: the impressed
current anode is connected via the DC power source to both the zinc anode and the
steel. This allows the re-charging process described at c) and the impressed current
described at b) to proceed concurrently.
[0116] The first two functions are well understood and need no further description. However
the arrangement, where both options are available (and operable) concurrently is novel.
[0117] The third function is novel with respect to the use of galvanic anodes for steel
reinforcement protection and involves making the zinc anode cathodic allowing deposition
of zinc. Zinc may be deposited from a number of zinc compounds and through various
reactions and is likely to include Reactions 1, 2 and 3 if zinc is in an alkaline
environment.
ZnO + 2OH
- + H
2O → Zn(OH)
42- (1)
Zn(OH)
42- → Zn
2+ + 4OH
- (2)
Zn
2+ + 2e
- → Zn (3)
[0118] Theoretically, all the zinc oxide and other zinc ions and zinc corrosion products
can be re-deposited on the core as usable zinc for subsequent consumption. In reality,
as with rechargeable alkaline batteries, the level of each subsequent recharge is
likely to be reduced.
[0119] A typical reaction at the impressed current electrode is likely to be:
2OH
- → ½O
2 + H
2O + 2e
- (4)
or
H
2O → ½O
2 + 2H
+ + 2e
- (5)
[0120] There is therefore a net balance of the hydroxyl ions which means there is no overall
loss in alkalinity within the assembly. There is a net increase in hydroxyl ions at
the surface of the zinc anode which is initially beneficial in accommodating large
amounts of the soluble zincate ions once the anode is used again, in galvanic mode,
to protect the steel reinforcement. The reaction at the impressed current anode (Eq
4 or 5) involves the production of oxygen gas which needs to escape from the assembly
and into the concrete pore structure. The impressed current anode, therefore, should
be porous, be in the form of a net or be vented.
[0121] A preferred way to employ the anode arrangement herein is to initially set it up
as a normal galvanic anode, allowing it to run for a period of say 10-20 years according
to exposure conditions. Occasional monitoring will determine when recharging of the
anode is required. An external power supply is then used to recharge the anode over
a relatively short period, preferably no more than 14 - 60 days. The anode is then
able to produce adequate current for a further period of time, say 5 - 20 years. The
process can be repeated several times until recharging becomes essentially ineffective.
If required, the impressed current part of the anode can then be simply used as part
of an impressed current corrosion protection system. Protection of the steel reinforcement
could therefore be achieved for the whole life of the structure.
[0122] The assembly has great flexibility which allows variable application types. For example,
a preliminary use of the impressed current part of the anode can deliver an initial
high level of charge over a limited period in order to passivate the steel to virtually
stop any ongoing corrosion. Alternatively, the impressed current part of the anode
can be operated to deliver a cumulative charge to increase the alkalinity of the concrete
surrounding the steel and reduce future corrosion and current demand from the galvanic
galvanic anode. Applied charge of 20,000 to 150,000 and more typically, 70,000 to
100,000 Coulombs per square meter of steel has been shown to be sufficient to passivate
the steel. Applied charges of around 700,000 Coulombs/m2 have been effective at re-alkalizing
(increasing the pH) of carbonated concrete. The charge required to increase the pH
of concrete which is not carbonated will be less than 700,000 Coulombs/m2. This can
then be followed by a lower level of galvanic current to maintain passivity of the
steel. Using the impressed current anode to deliver the high initial charge is beneficial
as this prevents unnecessary consumption and degradation of the sacrificial anode,
allows a smaller sacrificial anode to be used and allows the sacrificial anode to
provide higher current to the steel after the high initial charge has been passed
to the steel by the impressed current anode. Recharging of the anodes can still be
carried out if required. Furthermore, additional externally applied current can be
delivered via the impressed current anode of the assembly if steel passivity is lost,
if the current from the sacrificial anode is not sufficient to polarize the steel
or if either the corrosion potential or the corrosion rate of the steel increases
above desired levels. The assembly also has the capability to operate principally
as an impressed current anode with a rechargeable galvanic anode backup for periods
when the impressed current anode is off line or is otherwise non-functional. Similarly,
the impressed current anode can be available to operate as a backup to the sacrificial
anode should the sacrificial anode become non-functional.
[0123] In a preferred arrangement, the inert anode may be capable of delivering a high level
of current, possibly as high as 1mA/cm2. The resistance of the electrolyte is preferably
therefore as low as possible, so that a gel may be more suitable than a solid. Considerable
levels of oxygen gas can be produced during charging which needs to disperse adequately
through the anode walls and surrounding concrete.
[0124] In order for the anode to be rechargeable, the electrolyte is preferably highly alkaline.
This allows high concentrations of Zn(OH)
42- in solution after the dissolution of zinc which, with supersaturation, is believed
to precipitate out as ZnO. These reactions are believed to be as set out in Equations
5 and 6 below, which are essentially the reverse of Reactions 1 and 2.
Zn + 4OH
- → Zn(OH)
42- + 2e
- (6)
Zn(OH)
42- → ZnO + 2OH
- + H
2O (7)
[0125] Other electrolytes which are not highly alkaline are also suitable as long as soluble
or electrochemically mobile zinc ions are present.
[0126] Preferably the assembly includes sufficient moisture to be highly ionically conductive
and to allow sacrificial anode ions to be mobile during charging or recharging. Humectants,
gels and other hydroscopic materials can be beneficial in this regard. In an alternative
arrangement, charging or recharging of sacrificial anodes can be improved by applying
water or another wetting solution to at least a portion of the structure and or specifically
the sacrificial anode to keep it sufficiently conductive during the charging or recharging
process.
[0127] Testing has shown that zinc can be deposited onto many substrates including; zinc,
titanium, copper, steel and stainless steel. As such, partially discharged and fully
consumed sacrificial anodes can be regenerated.
Example 1
[0128] In one example, a cast zinc anode, 8cm long with a minimum diameter of 0.7cm, was
located in ZnO/thixotropic paste packed inside a conductive ceramic impressed current
anode tube. The zinc paste was made from a solution saturated with LiOH with 2M KOH
and 20% ZnO along with carboxymethyl cellulose sodium thickening agent. The paste
was packed in the space between the zinc anode and the inner side of the 28mm tube.
Testing has shown that ions can pass through the porous tube walls such that the zinc
anode can pass current onto the external steel reinforcing bar even though it is located
inside the impressed current anode. Subsequently, charging of the zinc can be accomplished
by reversing the flow of ions through the impressed current porous tubular anode by
applying an external voltage between the impressed current anode and the sacrificial
anode. An applied voltage of around 6-8 Volts resulted in a current of up to 1.6A
to be delivered to the inner zinc anode achieving a total charge / recharge of just
under 40,000 Coulombs. Surprisingly, the zinc anode performed better after recharging
than it did originally. After charging of the zinc anode, when the zinc anode was
reconnected to the steel, the current output and cumulative charge output of the recharged
zinc anode through the porous tubular impressed current anode to the steel was increased
compared to the original zinc anode. The exact reasons for this improvement in performance
are not known but the current output of the anode after charging is increased.
[0129] In Figure 8 shows an example of an anode apparatus 30 as previously described where
the apparatus includes a Cast Zinc Core 31 inside a 28mm diameter porous conductive
impressed current anode 32. An upper end is closed by an attached disk 33 forming
a porous form and a lower end is closed by a Porous Fabric Cap 36. Between the core
31 and the cylindrical anode 32 is provided a filler material of LiOH + 2M KOH + 20%
ZnO + carboxymethyl cellulose sodium 35. The core is attached to a steel wire 34 for
connection as described above.
[0130] Figure 9 is a graph of current output of the anode of Figure 8 to steel, a) with
the anode as originally made, b) with the anode after a period of charging via the
porous conductive impressed current anode.
[0131] Figure 10 is a graph of cumulative charge output of the anode to steel, a) with anode
as originally made, b) after a period of charging via the porous conductive tube.
Example 2
[0132] An assembly 49 to demonstrate the ability to charge/recharge an anode in situ was
constructed as shown in Figure 11. It consisted of a zinc wire 50 partly immersed
in a highly alkaline (7 molar OH-) gel 51. A copper wire connector 53 for the sacrificial
anode to be formed in situ was also immersed in the same gel. The gel was contained
within a perforated plastic tube 54 lined both internally and externally by a layer
of fibre fabric 55 and ionically conductive membrane 56. Between the external fabric
and the tube a mixed metal oxide (MMO) coated titanium mesh 57 was fixed circumferentially
and had a titanium connection wire 58 attached to one side. The whole assembly was
encased in a mortar 59 enriched with LiOH.
[0133] The anode assembly 49 was cast centrally in a cement mortar prism approximately 80mm
x 50mm x 40mm high ensuring that the whole assembly was encased within the cement
mortar 59. As shown in Figure 12, the prism was then placed in a larger container
61 filled almost to the height of the prism with an alkaline solution 60. An external
mesh 62 of MMO coated titanium was placed along the periphery of the container to
act as the metal section.
[0134] The zinc wire 50 was connected electrically to the external titanium mesh 62. The
assembly 49 was then seen to act as a galvanic anode passing current to the external
titanium mesh (metal section) and producing zinc corrosion products until all available
zinc was consumed.
[0135] An external power supply (not shown) was then connected to the internal MMO coated
titanium mesh anode 57 within the anode assembly 49 and the copper wire 53 ensuring
that the copper was cathodic. Zinc corrosion products from the consumed (corroded)
zinc wire 50 were deposited on the copper wire 53 to form a sacrificial anode during
this charging process. Subsequent connection of the copper wire 53, now carrying the
deposited zinc and the external MMO coated titanium mesh (metal section) allowed current
to pass between the charged anode 53 and the metal section 62. The current produced
by the charged anode (copper wire with deposited zinc) was comparable to the current
produced by the original zinc wire. Comparison of current produced by the original
'discharge' of the zinc wire and the zinc which was deposited on the copper wire is
shown in Table 1.
Table 1: Current output of original zinc wire and deposited zinc on copper wire
| |
Current output (mA) |
| |
Maximum |
Minimum |
Mean |
| Original zinc wire |
5.47 |
0.05 |
0.70 |
| Deposited zinc on Copper Wire |
5.20 |
0.05 |
0.51 |