Classifications

• • C—CHEMISTRY; METALLURGY
  • C23—COATING 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
  • C23F—NON-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
  • C23F13/00—Inhibiting corrosion of metals by anodic or cathodic protection
  • C23F13/02—Inhibiting corrosion of metals by anodic or cathodic protection cathodic; Selection of conditions, parameters or procedures for cathodic protection, e.g. of electrical conditions
  • C23F13/06—Constructional parts, or assemblies of cathodic-protection apparatus
  • C23F13/08—Electrodes specially adapted for inhibiting corrosion by cathodic protection; Manufacture thereof; Conducting electric current thereto
  • C23F13/20—Conducting electric current to electrodes
• • C—CHEMISTRY; METALLURGY
  • C23—COATING 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
  • C23F—NON-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
  • C23F13/00—Inhibiting corrosion of metals by anodic or cathodic protection
  • C23F13/02—Inhibiting corrosion of metals by anodic or cathodic protection cathodic; Selection of conditions, parameters or procedures for cathodic protection, e.g. of electrical conditions
  • C23F13/06—Constructional parts, or assemblies of cathodic-protection apparatus
• • C—CHEMISTRY; METALLURGY
  • C23—COATING 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
  • C23F—NON-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
  • C23F13/00—Inhibiting corrosion of metals by anodic or cathodic protection
  • C23F13/02—Inhibiting corrosion of metals by anodic or cathodic protection cathodic; Selection of conditions, parameters or procedures for cathodic protection, e.g. of electrical conditions
  • C23F13/06—Constructional parts, or assemblies of cathodic-protection apparatus
  • C23F13/08—Electrodes specially adapted for inhibiting corrosion by cathodic protection; Manufacture thereof; Conducting electric current thereto
  • C23F13/10—Electrodes characterised by the structure
• • C—CHEMISTRY; METALLURGY
  • C23—COATING 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
  • C23F—NON-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
  • C23F2201/00—Type of materials to be protected by cathodic protection
  • C23F2201/02—Concrete, e.g. reinforced
• • C—CHEMISTRY; METALLURGY
  • C23—COATING 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
  • C23F—NON-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
  • C23F2213/00—Aspects of inhibiting corrosion of metals by anodic or cathodic protection
  • C23F2213/20—Constructional parts or assemblies of the anodic or cathodic protection apparatus
  • C23F2213/21—Constructional parts or assemblies of the anodic or cathodic protection apparatus combining at least two types of anodic or cathodic protection
• • C—CHEMISTRY; METALLURGY
  • C23—COATING 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
  • C23F—NON-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
  • C23F2213/00—Aspects of inhibiting corrosion of metals by anodic or cathodic protection
  • C23F2213/20—Constructional parts or assemblies of the anodic or cathodic protection apparatus
  • C23F2213/22—Constructional parts or assemblies of the anodic or cathodic protection apparatus characterized by the ionic conductor, e.g. humectant, hydratant or backfill
• • E—FIXED CONSTRUCTIONS
  • E04—BUILDING
  • E04C—STRUCTURAL ELEMENTS; BUILDING MATERIALS
  • E04C5/00—Reinforcing elements, e.g. for concrete; Auxiliary elements therefor
  • E04C5/01—Reinforcing elements of metal, e.g. with non-structural coatings
  • E04C5/015—Anti-corrosion coatings or treating compositions, e.g. containing waterglass or based on another metal

Definitions

• This invention relates to corrosion protection using a sacrificial material.
• 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.
• 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.
• 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 steei. It is also known to provide solar panels for charging batteries to be used in a system of this type.
• 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.
• 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 over time.
• 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;
• 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.
• sacrificial anode ions are present in the ionically conductive material.
• the re-charging causes hydroxyl ions to be generated at the surface of the sacrificial anode.
• the re-charging causes an alkali environment to be regenerated around the sacrificial anode.
• 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.
• the DC power supply is applied temporarily.
• ions of the sacrificial material available to be deposited.
• the ions of the sacrificial material are soluble.
• the ions of the sacrificial material are electrochemically mobile.
• the metal section is steel and the ionically conductive material is concrete or mortar.
• a method for use in corrosion protection of a metal section in an ionically conductive covering material comprising:
• connection between the sacrificial anode and the metal section so that the sacrificial anode provides corrosion protection.
• connection between the sacrificial anode and the metal section remains in place when the DC power supply is in operation.
• At least a portion of the sacrificial anode is fabricated in the ionically conductive material by depositing ions of the sacrificial material
• 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.
• the second terminal of the DC power supply is connected to the sacrificial anode and to the metal section.
• 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.
• 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.
• 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.
• the impressed current anode and the sacrificial anode are electrically separated to prevent electrical communication therebetween.
• 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.
• the sacrificial anode forms a rod and the impressed current anode forms a sleeve surrounding the rod.
• the impressed current anode and the sacrificial anode comprise side by side plates.
• an ionically conductive filler material between the impressed current anode and the sacrificial anode.
• the ionically conductive filler material is different from the ionically conductive material.
• the ionically conductive filler material contains sacrificial anode ions
• the ionically conductive filler material is porous.
• the ionically conductive filler material is deformable.
• the ionically conductive filler material contains at least one activator to ensure continued corrosion of the sacrificial anode.
• the ionically conductive filler material is hydroscopic.
• 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.
• a plurality of sacrificial anodes and wherein the impressed current anode is separate from said sacrificial anodes.
• a plurality of impressed current anodes and wherein the sacrificial anode is separate from said impressed current anodes.
• the impressed current anode is arranged to be mounted temporarily to provide current through a surface of the ionically conductive material.
• sacrificial anode ions available to be deposited.
• the sacrificial anode ions are soluble.
• the sacrificial anode ions are electrochemically mobile.
• this arrangement is designed for use where the metal section is steel and the ionically conductive material is concrete or mortar. In some cases a portion of the structure or the sacrificial anode is wetted.
• the impressed current anode is mounted temporarily for the purpose of causing the ions of the sacrificial material to be deposited.
• anode apparatus for cathodically protecting a metal section in an ionically conductive material
• the anode apparatus comprising:
• 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;
• a first electrical connector arranged for connection to the sacrificial anode
• 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.
• 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.
• sacrificial anode ions may be deposited to create a sacrificial anode or to increase the size of an existing sacrificial anode.
• 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.
• 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.
• 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.
• the impressed current anode and the sacrificial anode should be electrically separated to prevent electrical communication therebetween
• 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.
• 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.
• 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.
• 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.
• 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.
• 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.
• 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.
• the apparatus preferably includes as a part of the apparatus a DC power supply with positive and negative terminals.
• 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.
• a suitable source of DC power must be used at least during a part of the time.
• 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.
• the impressed current anode is perforated so to allow passage of ionic current to pass through the impressed current anode.
• 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.
• 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.
• the impressed current anode can be perforated by macroscopic holes formed through or cut into the anode.
• 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 materia] and / or other materials or reducing oxides to form an electrically conductive matrix.
• 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.
• the sacrificial anode forms a rod and the impressed current anode forms a sleeve surrounding the rod.
• 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.
• 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.
• the ionically conductive filler material is in ionic contact with at least part of the surface of the sacrificial anode.
• the ionically conductive filler material preferably contains at least one activator to ensure continued corrosion of the sacrificial anode.
• 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.
• the ionically conductive filler materia! 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.
• 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.
• 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.
• 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.
• 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.
• 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 concurrentiy.
• 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.
• 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.
• 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.
• 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.
• the sacrificial anode may be any of the more electro-negative materials such as zinc, aluminum, magnesium or alloys thereof.
• 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.
• the power supply is a battery it can be rechargeable.
• 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.
• 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.
• a method for corrosion protection of a metal section in an ionica!ly conductive covering material comprising:
• 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.
• 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.
• 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.
• 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.
• 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.
• the initial current provided by the impressed current anode is sufficient to passivate the metal section.
• the specific effect obtained in the first step is not essential and other effects can be obtained advantageously using this method.
• 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.
• separate anode elements can be provided.
• the impressed current anode and the sacrificial anode are electrically separated to prevent electrical communication therebetween.
• 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.
• 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.
• the sacrificial anode forms a rod and the impressed current anode forms a sleeve surrounding the rod.
• other arrangements can be provided such as parallel or side by side plates.
• an ionically conductive filler material adjacent to the sacrificial anode where the ionically conductive filler material is different from said ionically conductive material.
• the ionically conductive filler material contains at least one activator to ensure continued corrosion of the sacrificial anode.
• activator to ensure continued corrosion of the sacrificial anode.
• Many different types of activator are available and can be used.
• 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.
• a plurality of impressed current anodes and wherein the sacrificial anode is separate from said impressed current anodes.
• the sacrificial anode and the impressed current anodes are parts of a common construction.
• 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.
• 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.
• 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.
• 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.
• 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.
• 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 1 is shown a covering material 10 within which is embedded steel material 11 and an anode body 12.
• 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.
• 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.
• a DC power supply 14 is provided which generates a voltage at terminals 15 and 16 of the power supply.
• 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.O 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.
• 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.
• 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 0 located as a cylinder between the impressed current anode 21 and the sacrificial anode 20.
• 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.
• 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.
• 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.
• 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.
• 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.
• 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.
• 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.
• 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.
• 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 21 A are formed as two parallel plates, mesh, ribbon or wires with the filler material 22A therebetween.
• the re-charging of the sacrificial anode may occur primarily on one side.
• the two parallel layers of plates or mesh may be applied to the surface of the covering material.
• FIG. 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.
• 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.
• the second terminal can be connected to the steel if the protection of the steel is intended to continue during the re-charging process.
• 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.
• junction box 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.
• 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.
• 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.
• the assembly has great flexibility which allows variable application types.
• 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.
• 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.
• 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.
• the impressed current anode can be available to operate as a backup to the sacrificial anode should the sacrificial anode become non-functional.
• the inert anode may be capable of delivering a high level of current, possibly as high as 1 mA/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.
• the electrolyte is preferably highly alkaline. This allows high concentrations of Zn(OH)4 2" 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.
• electrolytes which are not highly alkaline are also suitable as long as soluble or electrochemically mobile zinc ions are present.
• 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.
• 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.
• 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.
• 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.
• the zinc anode performed better after recharging than it did originally.
• 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.
• 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 to steel, a) with anode as originally made, b) after a period of charging via the porous conductive tube.
• Example 2
• 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.
• MMO mixed metal oxide
• 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.
• 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.
• Table 1 Current output of original zinc wire and deposited zinc on copper wire

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