ELECTROCHEMICAL METHOD AND ELECTRODE

Abstract: An electrochemical electrode comprises a tube of porous titanium suboxide, and contains a contact for connection to an electrical supply.

Description: ELECTROCHEMICAL METHOD AND ELECTRODE The mvention relates to an electrochemical method and an electrode thereof. The invention can be applied to a wide variety of uses. It is particularly effective in the treatment of reinforced concrete. Such concrete comprises a steel bar reinforcing framework swithin a body of set concrete. Other uses will be described below. It is known to connect such framework to a source of direct current to apply a voltage sufficient to maintain the metal in a corrosion resistant state, to avoid or treat corrosion. Such a system is called cathodic protection. Generally this technique utilises a distributed anode system such as metal mesh, or conductive coatings such as paints and speciality gunited and sprayed material. There are however some areas which cannot be addressed in this way and "discrete" or "point" anodes are suggested. There are already two basic types of point anodes on the market, the most common being a platinised titanium rod. The other type is generally a shaped titanium mesh or titanium metal tube or plate, catalysed with an appropriate or mixed metal oxide based material. The platinised titanium rod cannot be used alone however, because at the current ratings required (which are controlled by the density of the steel bars in the vicinity), the current density at the anode surface would be very high, generating acid at a rate far faster than it could diffuse away (and ultimately be neutralised by the alkali generated on the cathodic reinforcing bars). Hence the concrete would be destroyed by acid attack in the neighbourhood of the anode. The US National Association of Corrosion Engineers have a guideline that the current density should be no higher than 100mA./m 2 of concrete area to avoid this phenomenon. The rod is usually put in a significantly larger hole (typically 12 mm diameter) than would otherwise be required and the void is filled with a carbon based conductive paste to increase the surface area and hence reduce the current density at the concrete surface. For cost reasons however they still tend to be run well above the NACE guidelines. At current densities above 0.3mA.cm length (about 800mA m 2 ) the carbon backfill is consumed by anodic oxidation forming CO 2 . As a result the contact between the carbon and the concrete is lost and the voltage to drive the protecting current rises, often outstripping the rating of the rectifier. In addition to this though, other mechanisms are possibly taking place. The high current flows generate gases, typically oxygen with traces of chlorine or carbon dioxide from the oxidation of the carbonaceous paste at the anode surface and this may have difficulty escaping, causing blowholes further reducing the contact at the concrete surface. (It is known that at very high current densities (around 15A.m 2 ) the anodes can "gas block" within hours of being powered up.) Generally, because of the need to attend to a specialised conductive carbonaceous grout, the rod is restricted to anodes near the surface. Often there is steel work buried deep within the structure which would be assisted with a local anode close by. It is an object of the invention to provide a more convenient and advantageous point electrode for use in the treatment of reinforced concrete and other electrochemical applications. In one aspect the invention provides an electrochemical electrode for use in electrochemical treatment of reinforced concrete or the like, the electrode comprising a wall comprising a porous material having an external and internal surface, a supply conductor being, in use, in electrical contact with the internal surface and with a supply of electric current. The wall may be of any appropriate three dimensional shape, typically a cylinder or sphere. Because the connection of the conductor is connected to the internal surface of the wall anodic corrosion is avoided. The external surface will be corrosion resistant. The wall is preferably shaped so that the electrode is tubular, i.e. open at both ends to define a gas transfer passage or channel. The wall is porous to allow for ingress of gas into the passage; the porosity is selected so that any later applied grout or back filling does not significantly impede the gas passage. Preferably the wall is formed of a porous titanium suboxide. Preferably the titanium suboxide is of the formula TiO x where x is 1.55 to 1.95. As indicated below, other porous materials may be used, and the electrode assembly may be used for other electrochemical processes. Preferably the conductor extends through a bore in the electrode, e.g. through end caps in a generally cylindrical form. Most preferably a sheath extends beyond each end of the cylinder to convey released gases away from the electrode surface. In another aspect, the invention provides a method for electrochemical treatment of reinforced concrete or the like, the method comprising exposing the reinforcement, locating an electrode adjacent a selected portion of the reinforcement, the electrode comprising a wall formed of porous material and having an external and internal surface, and connecting the internal surface of the wall to a supply of electric current. Preferably the internal surface of the wall is connected to a suppiy conductor connected to the supply of electric current. The method preferably uuis passing the conductor through the electrode, and through a sheath extending beyond each end of the electrode. Preferably the hole drilled in the concrete is dimensioned much the same as the electrode (because there is no need to increase the surface area by including a body of conductive paste). The advantages of the electrode of the invention are that it offers an effective but simple connection method to any tubular anode. Being tubular the Faradaic field inside the tube is insignificant and there is therefore no driving force for anodic corrosion of the metal within the tube. The metal inside the tube can therefore be selected solely on chemical corrosion considerations. Detailed electrode designs according to the invention can be very simple and fabricated in the field. In one embodiment all that is required is a spot welder and an insertion tool. This means that the electrodes can be located on-site after comparison with the actual layout of the holes and reinforcing bars, in the case of anodes for cathodic protection. Because special conductive grouts are not needed and the gas generated by the anodic reaction can easily be removed from the anode surface, the electrodes can be located deep down holes and back-filled with a conventional pumpable grout, which will not need replacing, especially if it has a high content of alkali or other reactant for the concrete. The connection system also means that more than one electrode can be attached to the supply conductor, e.g. a feeder wire, enabling current to be distributed at different depths down the hole. This has the advantage of ensuring the cathodic current density does not get too high which would cause hydrogen embrittlement of the steel bars. Other options are ring-mains of electrodes and horizontal strings let into channels of slabs and soffits; and the like. Such strings and ring mains may also be useful in protecting such items as underground pipelines or storage vessels. Such electrode assemblies may be useful in other electrochemical techniques such as in-situ remediation and in general. The most obvious advantage however, is that by provision of a suitable sheath, the anodic gases can be safely conducted away along the line of the feed wire, reducing the probability of loss of electrical contact from this cause, especially at high current densities. This device is not only applicable to titanium suboxide but elements of it are applicable to any cylindrical/spherical perhaps porous structure (e.g. titanium metal foam - incorporating an electrocatalyst). The cylinders can be made in a variety of dimensions to adjust the current density appropriately. So by ease of adjusting the current density, lack of consumed carbonaceous backfill, ability to remove the gaseous products, abihty to install alkalinity grouts (these last three items indicating the possibility of higher current densities being tolerated) and flexibility of anode location the invention is particularly useful. Other advantages of the invention are that: 1. the internal connection inside a tube eliminates anodic corrosion of the connector; 2. ease of assembly and flexibility of design; 3. provides facilities for gas removal; and 4. simplicity of contact allowing for several anodes on one string. In order that the invention may be well understood it will now be described by way of example with reference to the accompanying diagrammatic drawings, in which: Figure 1 is a longitudinal section through one anode of the mvention; and Figure 2 is a view from one end of the anode; Figure 3 is a longitudinal section through another anode of the invention; and Figure 4 is a cross section of a body of concrete being treated by a method according to the invention. The anode comprises a cylinder 1 having a wall formed of porous material, typically a titanium suboxide of the general formula TiO x where x is 1.55 to 1.95. (Such material can be made by any process of our patents, e.g. EP-A-0047595 and EP-A-0478152, provided that care is taken to induce porosity). The cylinder contains end caps 2 containing through bores 3. The cylinder 1 also contains a connector 4, made of sihcon rubber or the like having a bore 5 and which carries a strip 6 of typically titanium metal, and which presses it against the internal surface of the cylinder 1. The strip is connected typically by spot welding to a feeder wire 7, extending through the cylinder and connected to a source of electric current (not shown). The feeder wire is housed in sheath 8. typically of a plastic material, beyond the cylinder. One such cylinder may be connected to another so that a ladder of such anodes is formed (see Figure 4), each anode being associated with a different area of the reinforcement. The arrangement of the end plugs and connector may be varied as shown in the embodiment of Figure 3. One end cap can be replaced by a cap without a through bore for the single final anode in a ladder assembly. In use and as shown in Figure 4, a hole H is drilled in the concrete C, not shown, to reach the reinforcement R to be protected, the hole being only slightly larger in diameter than the electrode cylinder. The depth of the hole is determined by the geometry of the reinforcing bars in the concrete structure. The electrode is assembled by fitting the end caps in position and then inserted into the hole. The anode is then connected to the supply of direct current. The hole is filled with grout G. When gases are evolved by the chemical reactions they can escape into the cylinder and up through the plastic sheath 8 to the atmosphere. In this way they do not contact the concrete and hence do not influence the current carrying capacity of the electrode. As shown a vertical string of the anodes is formed. The mvention is not limited to the embodiment shown. For example the end caps may be omitted, and the method of connecting the feeder wire to the internal surface of the cylinder or other three dimensionally shaped electrode may be varied.

Claims: CLAIMS 1. An electrochemical electrode for use in an electrical treatment of reinforced concrete or the like, the electrode comprising a wall comprising a porous material having an external and internal surface, a supply conductor being, in use, in electrical contact with the internal surface and with a supply of electric current. 2. An electrode according to Claim 1 , wherein the wall is formed of a porous titanium suboxide. 3. An electrode according to Claim 2, wherein the titanium suboxide is of the formula TiO x where x is 1.55 to 1.95. 4. An electrode according to any preceding Claim, wherein the conductor extends through the electrode. 5. An electrode according to any preceding Claim, in generally cylindrical form. 6. An electrode according to any preceding Claim 5, wherein a sheath extends beyond each end of the cylinder to convey released gases. 7. A method for electrochemical treatment of reinforced concrete or the like, comprising exposing the reinforcement, locating an electrode adjacent a selected portion of the reinforcement, the electrode comprising a wall formed of porous material and having an external and internal surface, and connecting the internal surface of the wall to a supply of electric current. 8. A method according to Claim 7, wherein the internal surface of the wall is connected to a supply conductor connected to the supply of electric current. 9. A method according to Claim 7 or 8, wherein the electrode is of generally cylindrical form, including passing the conductor through the cylinder, and through a sheath extending beyond each end of the cylinder. 10. A method according to any of Claims 7 to 9. wherein the reinforcement is approached by forming a hole in the set concrete and the hole is dimensioned to coπespond substantially to the dimensions of the electrode.

Inventors: HAYFIELD PETER CHARLES STEELE, HILL ANDREW, HAYFIELD, PETER, CHARLES, STEELE, HILL, ANDREW
Applicants: ATRAVERDA LTD, HAYFIELD PETER CHARLES STEELE, HILL ANDREW, ATRAVERDA LIMITED, HAYFIELD, PETER, CHARLES, STEELE, HILL, ANDREW
Application year: 1997
Main classification: C23F13
IPC codes: C23F13