EP2809830A1 - Device for the cathodic protection of a metal wall against corrosion in a saline environment - Google Patents

Device for the cathodic protection of a metal wall against corrosion in a saline environment

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Publication number
EP2809830A1
EP2809830A1 EP13705736.0A EP13705736A EP2809830A1 EP 2809830 A1 EP2809830 A1 EP 2809830A1 EP 13705736 A EP13705736 A EP 13705736A EP 2809830 A1 EP2809830 A1 EP 2809830A1
Authority
EP
European Patent Office
Prior art keywords
anode
wall
compartment
metal wall
cation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP13705736.0A
Other languages
German (de)
French (fr)
Inventor
Serge Prigent
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GE Renewable Technologies Wind BV
Original Assignee
Alstom Renewable Technologies Wind BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Alstom Renewable Technologies Wind BV filed Critical Alstom Renewable Technologies Wind BV
Publication of EP2809830A1 publication Critical patent/EP2809830A1/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F13/00Inhibiting corrosion of metals by anodic or cathodic protection
    • C23F13/02Inhibiting corrosion of metals by anodic or cathodic protection cathodic; Selection of conditions, parameters or procedures for cathodic protection, e.g. of electrical conditions
    • C23F13/06Constructional parts, or assemblies of cathodic-protection apparatus
    • C23F13/08Electrodes specially adapted for inhibiting corrosion by cathodic protection; Manufacture thereof; Conducting electric current thereto
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F13/00Inhibiting corrosion of metals by anodic or cathodic protection
    • C23F13/02Inhibiting corrosion of metals by anodic or cathodic protection cathodic; Selection of conditions, parameters or procedures for cathodic protection, e.g. of electrical conditions
    • C23F13/06Constructional parts, or assemblies of cathodic-protection apparatus
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F2201/00Type of materials to be protected by cathodic protection
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F2213/00Aspects of inhibiting corrosion of metals by anodic or cathodic protection
    • C23F2213/30Anodic or cathodic protection specially adapted for a specific object
    • C23F2213/31Immersed structures, e.g. submarine structures

Definitions

  • the invention relates to the cathodic protection of immersed installations in a brackish or saline environment.
  • a sacrificial anode consisting of a more electronegative metal than the one to be protected.
  • a polarization occurs, the shell becoming the cathode of an electrochemical cell and the sacrificial anode becoming the anode of the same cell.
  • M constituents of the sacrificial anode that undergo the effects of corrosion by seawater and not those of the shell.
  • Sacrificial anodes protecting the submerged steel parts of a boat or other fixed gear are usually aluminum-zinc (2-6%) - indium (0.01-0.05%), or aluminum -gallium (0.01%) or zinc alloy-AI (0.1 -0.5%).
  • the disadvantage of this protection is that it releases in the marine environment ions of the metals constituting the sacrificial anodes. If this disadvantage is relatively minimal in the case of boats moving on the open sea, it is to be considered significantly more seriously when the boats are immobilized in a port, because the metals of the anode will accumulate in the water and in the water. the seabed of the parking areas, where they are going to be absorbed by the living beings who stay there.
  • the object of the invention is to provide a solution for preventing the release into the external environment of the cations resulting from the dissolution of an anode of a cathodic protection device.
  • the subject of the invention is a device for cathodic protection of a metal wall against corrosion in a salt medium, comprising an anode and means for connecting said anode to said wall, said anode being at an electrochemical potential. higher than said wall, characterized in that said anode is placed in a compartment delimited by an electron-permeable wall and, possibly, water, comprising:
  • porous outer layer made of a material chosen from: polymer materials, ceramic materials or hydrated inorganic materials;
  • the material constituting said at least one layer being chosen from osmotic membranes, activated carbon, a cation exchange resin such as a zeolite, a nano-cations cation-capturing polymer, cation-capturing mineral compounds such as phyllosilicates and inosilicates, microporous organic semi-permeable nanofiltration membranes of a cation-retaining type.
  • Said wall may also include a membrane trapping negatively charged contaminants.
  • the anode may be a sacrificial anode whose electrochemical potential is naturally greater than that of the metal wall.
  • the device may comprise means for imposing on the anode an electrochemical potential greater than that of the metal wall.
  • connection means of the anode to the metal wall may be in contact with the wall outside the compartment and pass through the porous wall of the compartment.
  • the means for connecting the anode to the metal wall may be in contact with the metal wall inside the compartment, and the porous wall of the compartment is sealingly connected to the metal wall.
  • the device may comprise means for keeping the anode away from the metal wall. It may comprise a plurality of layers having the capacity to capture the cations emitted by the anode during its dissolution, each layer preferably capturing cations different from those picked up in a preferred manner by the other layers.
  • the invention consists in placing the anode in a compartment delimited by a series of porous membranes permeable to at least electrons, or even to water, arranged in layers.
  • the outer layer is constituted by a porous non-metallic membrane, intended to reduce the hydraulic flow in the vicinity of the anode.
  • the other porous layer (s) act as a cation barrier or trap, which prevents cations from dissolution of the anode from escaping out of the compartment into the external environment.
  • the membranes are all permeable to water, the space between the anode and the wall of the compartment fills with water naturally. If at least one of the membranes is not permeable to water but only to electrons, it is necessary, during installation of the device, to fill the compartment with water, preferably with water. seawater to obtain good electrical conductivity, in order to bathe the anode in an electron-conducting medium and to give the compartment its operational form, with internal and external pressures that balance out.
  • a sacrificial anode 3 is disposed in the vicinity of the wall 1, to which it is connected by electrical connectors 4, 5.
  • the sacrificial anode 3 is made around a single steel connector, and in this case, the connectors 4, 5 shown are in fact the two ends of this single connector.
  • the constituent material of the sacrificial anode 3 is conventional for this purpose (Al-In, Al-Ga or Zn alloy for example), and its choice is not a characteristic of the invention.
  • the sacrificial anode 3 is included in a compartment 6 which is delimited by a set of membrane forming layers, and surrounds the anode 3 at a distance, for example, of the order of 1 cm.
  • the outermost layer 7 is a porous electron-permeable layer and, preferably, also water, intended to reduce the hydraulic flow between the external environment and the interior space 8 of the compartment.
  • the material constituting it is selected from polymeric materials, ceramic materials or hydrated inorganic materials.
  • thermoplastic polymers of the polyethylene or high density polyethylene type or industrial mullite or alumina type porcelains.
  • this material is electrically insulating, it must have porosity. Indeed, the polarization of the anode corresponds to the establishment of a small electrochemical circuit, which can only work if the electrons circulate. The open porosity allows the electrons to pass into the liquid even though the layer 7 is insulating.
  • This outermost layer 7 whose thickness is generally of the order of mm, serves to protect the anode and the other membranes of the compartment 6 against hydraulic abrasion. It must have suitable properties of resistance to wear and impacts, resistance to deformation in the presence of a fluid in motion.
  • the permeability of the layer 7 is, for example, of the order of 10 ml / min for 1 cm 2 of anode surface.
  • the other layer or layers of the wall of the compartment 6 (there are two, 9, 10, in the example shown) is or consist of one or more materials serving as cation traps, and which capture the cations emitted by the sacrificial anode 3 to prevent them from being found in the marine environment 2.
  • materials may be suitable: osmotic membranes, activated carbon powder or granules, a cation exchange resin such as a zeolite, a cation-attracting negative nanocharging cationic polymer, mineral cation-capturing compounds such as phyllosilicates and inosilicates.
  • osmotic membranes activated carbon powder or granules
  • a cation exchange resin such as a zeolite
  • a cation-attracting negative nanocharging cationic polymer such as phyllosilicates and inosilicates.
  • mineral cation-capturing compounds such as phyllosilicates and inosilicates.
  • An activated alumina membrane or a functionally equivalent compound can be added to them, which in turn traps negatively charged contaminants, such as As and fluorides, that could decrease the efficiency of cation-trapping membranes.
  • Semipermeable membranes used in electrolytic ion exchange processes can also be used.
  • Microporous organic semi-permeable nanofiltration membranes of a cation-retaining type may also be suitable.
  • the number of layers of cation sensor materials can be arbitrary, at the user's choice. These layers may advantageously be of multiple natures, each layer species being able, for example, to preferentially absorb one or more of the chemical species that the sacrificial anode 3 is capable of releasing.
  • the thickness of the layers, in particular of the layer 10, can vary from about 1 mm to a few cm, depending on the size of the anode 3 and, therefore, the amount of cations to trap.
  • compartment 6 In the case where the entire wall defining the compartment 6 is permeable to water, the water penetrates inside the compartment 6 and a pressure balance is reached between the inside and the outside of the compartment 6 The compartment 6 thus permanently takes its nominal form and its wall does not undergo crushing which could lead to its rupture.
  • the entire wall defining the compartment 6 is permeable to water. It may be permeable only to electrons, but then pre-filling compartment 6 with water, preferably seawater, is necessary during commissioning of the device according to the invention.
  • the progressive dissolution of the sacrificial anode 3 is carried out without pollution of the external medium by the cations resulting from this dissolution, these being captured by the layer or layers 9, 10.
  • These must have advantageously a total absorption capacity of the various cations and an absorption volume sufficient to not reach saturation before the end of life of the sacrificial anode 3.
  • the electrical conductors 4, 5 are in contact with the metal wall 1 in areas outside the compartment 6. It is necessary to therefore ensure a sealing of the wall of the compartment 6 in the areas where it is crossed by the conductors 4, 5. But alternatively, as shown in Figure 2, the contacts between the conductors 5, 6 and the metal wall 1 may be located inside the compartment 6. The wall of the compartment 6 is then in sealing contact with the metal wall 1 to be protected.
  • the sacrificial anode 3 is not in direct contact with the wall 1 to be protected. This avoids creating short circuits between the anode 3 and at least the area of the wall 1 which is opposite it. In this way, a greater part of the surface of the wall 1 can be protected under the best conditions by the same anode 3.
  • Means for holding the anode 3 away from the wall 1 are therefore provided, preferably (not shown in the figures). But in practice, they can often be constituted by the connectors 4, 5, which are generally made of steel and have due to their material and their dimensions, a sufficient rigidity to achieve the maintenance of the anode 3 at a distance from the wall 1.
  • the invention is also applicable in the case where the anode is not a sacrificial anode in the sense that it naturally has a higher electrochemical potential than that of the wall 1 to be protected, but is placed at this potential by a DC or rectified current generator to which it is connected by conductors which pass through the wall of the compartment 6 sealingly.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Prevention Of Electric Corrosion (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

A device for the cathodic protection of a metal wall (1) against corrosion in a saline environment, comprising an anode and means (4, 5) for connecting said anode to said wall (1), said anode having a higher electrochemical potential than said wall (1), characterised in that said anode is placed in a compartment (6) delimited by a wall permeable to electrons and, optionally, to water, comprising: - a porous outer layer (7) made from a material selected from: polymeric materials, ceramic materials or hydrated inorganic materials; - and at least one porous layer (9, 10) having the ability to collect the cations emitted by the anode during the dissolution of same, the material forming said at least one layer being selected from osmotic membranes, active carbon, a cation exchange resin such as a zeolite, a cation-collecting polymer with nanofillers, cation-collecting mineral compounds such as phyllosilicates and inosilicates, cation-retaining nanofiltering semi-permeable organic microporous membranes.

Description

Dispositif de protection cathodique d'une paroi métallique contre la  Device for cathodic protection of a metal wall against the
corrosion dans un milieu salin  corrosion in a saline environment
L'invention concerne la protection cathodique des installations immergées dans un milieu saumâtre ou salin. The invention relates to the cathodic protection of immersed installations in a brackish or saline environment.
La protection des coques métalliques de bateaux ou des parties métalliques contre la corrosion par l'eau de mer est, de façon classique, souvent assurée par une anode sacrificielle, constituée par un métal plus électronégatif que celui qui est à protéger. Lorsque le bateau et son anode sacrificielle sont immergés dans l'eau de mer, une polarisation intervient, la coque devenant la cathode d'une cellule électrochimique et l'anode sacrificielle devenant l'anode de cette même cellule. En conséquence, ce sont les constituants métalliques de l'anode sacrificielle qui subissent les effets de la corrosion par l'eau de mer et non ceux de la coque. Ces constituants M sont libérés dans l'eau de mer sous forme de cations selon la réaction M→ Mn+ + n e . The protection of metal hulls of boats or metal parts against corrosion by seawater is conventionally often provided by a sacrificial anode, consisting of a more electronegative metal than the one to be protected. When the boat and its sacrificial anode are immersed in seawater, a polarization occurs, the shell becoming the cathode of an electrochemical cell and the sacrificial anode becoming the anode of the same cell. As a result, it is the metal components of the sacrificial anode that undergo the effects of corrosion by seawater and not those of the shell. These constituents M are released in seawater in the form of cations according to the reaction M → M n + + ne.
Les anodes sacrificielles protégeant les parties immergées en acier d'un bateau ou de tout autre engin navigant ou installation fixe sont généralement en aluminium-zinc (2-6%)-indium (0,01 -0,05%), ou en aluminium-gallium (0,01 %) ou en alliage de zinc-AI (0,1 -0,5%). L'inconvénient de cette protection est qu'elle relâche dans le milieu marin des ions des métaux constituant les anodes sacrificielles. Si cet inconvénient est relativement minime dans le cas de bateaux se déplaçant en pleine mer, il est à considérer sensiblement plus sérieusement lorsque les bateaux sont immobilisés dans un port, car les métaux de l'anode vont s'accumuler dans l'eau et dans les fonds marins des zones de stationnement, où ils vont être absorbés par les êtres vivants qui y séjournent. Le problème se pose aussi pour les installations fixes telles que les plateformes pétrolières et les éoliennes « off-shore ». Il est donc impératif de trouver des solutions efficaces et économiques permettant d'éviter autant que possible cette libération de métaux nocifs dans le milieu extérieur, d'autant que les évolutions de la législation sur la protection environnementale pourraient rendre l'utilisation de solutions de maîtrise des rejets d'anodes sacrificielles obligatoire dans certaines circonstances.  Sacrificial anodes protecting the submerged steel parts of a boat or other fixed gear are usually aluminum-zinc (2-6%) - indium (0.01-0.05%), or aluminum -gallium (0.01%) or zinc alloy-AI (0.1 -0.5%). The disadvantage of this protection is that it releases in the marine environment ions of the metals constituting the sacrificial anodes. If this disadvantage is relatively minimal in the case of boats moving on the open sea, it is to be considered significantly more seriously when the boats are immobilized in a port, because the metals of the anode will accumulate in the water and in the water. the seabed of the parking areas, where they are going to be absorbed by the living beings who stay there. The problem also arises for fixed installations such as offshore oil platforms and wind turbines. It is therefore imperative to find effective and economical solutions to avoid as much as possible the release of harmful metals in the external environment, especially as changes in the environmental protection legislation could make the use of control solutions possible. mandatory sacrificial anode discharges under certain circumstances.
Une solution alternative à l'utilisation d'une anode sacrificielle telle qu'on vient de la décrire est de réaliser cette anode en un matériau non forcément plus électropositif que le matériau à protéger (ce peut être de l'acier, de la fonte, du graphite, des oxydes métalliques...), mais auquel on impose, de façon constante ou cyclique, un potentiel électrique au moyen d'un générateur de courant continu ou redressé. Ce potentiel rend l'anode plus apte à être corrodée que la paroi à protéger. Cette technique est lourde à mettre en place, surtout dans des zones de l'installation qui sont difficiles d'accès, mais est efficace pour des installations de grande taille principalement. Cette technique est connue sous le nom de « protection cathodique à courant imposé » (PCCI en abrégé). An alternative solution to the use of a sacrificial anode as just described is to make this anode in a material not necessarily more electropositive than the material to be protected (it can be steel, cast iron, graphite, metal oxides ...), but to which is imposed, constantly or cyclically, an electric potential by means of a DC generator or rectified. This potential makes the anode more likely to be corroded than the wall to be protected. This technique is cumbersome to implement, especially in areas of the facility that are difficult to access, but is effective for large installations mainly. This technique is known as "cathodic current protection" (abbreviated PCCI).
Le but de l'invention est de proposer une solution permettant d'éviter la libération dans le milieu extérieur des cations résultant de la dissolution d'une anode d'un dispositif de protection cathodique.  The object of the invention is to provide a solution for preventing the release into the external environment of the cations resulting from the dissolution of an anode of a cathodic protection device.
A cet effet, l'invention a pour objet un dispositif de protection cathodique d'une paroi métallique contre la corrosion dans un milieu salin, comportant une anode et des moyens de connexion de ladite anode à ladite paroi, ladite anode étant à un potentiel électrochimique plus élevé que ladite paroi, caractérisé en ce que ladite anode est placée dans un compartiment délimité par une paroi perméable aux électrons et, éventuellement, à l'eau, comportant :  For this purpose, the subject of the invention is a device for cathodic protection of a metal wall against corrosion in a salt medium, comprising an anode and means for connecting said anode to said wall, said anode being at an electrochemical potential. higher than said wall, characterized in that said anode is placed in a compartment delimited by an electron-permeable wall and, possibly, water, comprising:
- une couche extérieure poreuse en un matériau choisi parmi : des matériaux polymères, des matériaux céramiques ou des matériaux inorganiques hydratés ;  a porous outer layer made of a material chosen from: polymer materials, ceramic materials or hydrated inorganic materials;
- et au moins une couche poreuse ayant la capacité de capter les cations émis par l'anode lors de sa dissolution, le matériau constituant ladite au moins une couche étant choisi parmi des membranes osmotiques, du charbon actif, une résine échangeuse de cations telle qu'une zéolite, un polymère capteur de cations à nanocharges, des composés minéraux capteurs de cations tels que des phyllosilicates et des inosilicates, des membranes microporeuses organiques semi-perméables de nanofiltration d'un type retenant les cations.  and at least one porous layer having the capacity of capturing the cations emitted by the anode during its dissolution, the material constituting said at least one layer being chosen from osmotic membranes, activated carbon, a cation exchange resin such as a zeolite, a nano-cations cation-capturing polymer, cation-capturing mineral compounds such as phyllosilicates and inosilicates, microporous organic semi-permeable nanofiltration membranes of a cation-retaining type.
Ladite paroi peut comporter également une membrane piégeant les contaminants chargés négativement.  Said wall may also include a membrane trapping negatively charged contaminants.
L'anode peut être une anode sacrificielle dont le potentiel électrochimique est naturellement supérieur à celui de la paroi métallique.  The anode may be a sacrificial anode whose electrochemical potential is naturally greater than that of the metal wall.
Sinon, le dispositif peut comporter des moyens pour imposer à l'anode un potentiel électrochimique supérieur à celui de la paroi métallique.  Otherwise, the device may comprise means for imposing on the anode an electrochemical potential greater than that of the metal wall.
Les moyens de connexion de l'anode à la paroi métallique peuvent être au contact de la paroi à l'extérieur du compartiment et traversent de façon étanche la paroi poreuse du compartiment.  The connection means of the anode to the metal wall may be in contact with the wall outside the compartment and pass through the porous wall of the compartment.
Les moyens de connexion de l'anode à la paroi métallique peuvent être au contact de la paroi métallique à l'intérieur du compartiment, et la paroi poreuse du compartiment est connectée de manière étanche à la paroi métallique.  The means for connecting the anode to the metal wall may be in contact with the metal wall inside the compartment, and the porous wall of the compartment is sealingly connected to the metal wall.
Le dispositif peut comporter des moyens pour maintenir l'anode à distance de la paroi métallique. Il peut comporter une pluralité de couches ayant la capacité de capter les cations émis par l'anode lors de sa dissolution, chaque couche captant de façon privilégiée des cations différents de ceux captés de façon privilégiée par les autres couches. The device may comprise means for keeping the anode away from the metal wall. It may comprise a plurality of layers having the capacity to capture the cations emitted by the anode during its dissolution, each layer preferably capturing cations different from those picked up in a preferred manner by the other layers.
Comme on l'aura compris, l'invention consiste à placer l'anode dans un compartiment délimité par une série de membranes poreuses perméables au moins aux électrons, voire aussi à l'eau, disposées en couches. La couche extérieure est constituée par une membrane non-métallique poreuse, destinée à réduire le flux hydraulique au voisinage de l'anode. La ou les autres couches poreuses joue(nt) le rôle d'une barrière ou d'un piège à cations, qui empêche les cations issus de la dissolution de l'anode de s'échapper hors du compartiment dans le milieu extérieur.  As will be understood, the invention consists in placing the anode in a compartment delimited by a series of porous membranes permeable to at least electrons, or even to water, arranged in layers. The outer layer is constituted by a porous non-metallic membrane, intended to reduce the hydraulic flow in the vicinity of the anode. The other porous layer (s) act as a cation barrier or trap, which prevents cations from dissolution of the anode from escaping out of the compartment into the external environment.
Si les membranes sont toutes perméables à l'eau, l'espace séparant l'anode de la paroi du compartiment se remplit d'eau naturellement. Si au moins l'une des membranes n'est pas perméable à l'eau mais seulement aux électrons, il est nécessaire, lors de l'installation du dispositif, de réaliser un remplissage du compartiment par de l'eau, de préférence par de l'eau de mer pour obtenir une bonne conductivité électrique, afin de faire baigner l'anode dans un milieu conducteur des électrons et de conférer au compartiment sa forme opérationnelle, avec des pressions interne et externe qui s'équilibrent.  If the membranes are all permeable to water, the space between the anode and the wall of the compartment fills with water naturally. If at least one of the membranes is not permeable to water but only to electrons, it is necessary, during installation of the device, to fill the compartment with water, preferably with water. seawater to obtain good electrical conductivity, in order to bathe the anode in an electron-conducting medium and to give the compartment its operational form, with internal and external pressures that balance out.
L'invention sera mieux comprise à la lecture de la description qui suit, donnée en référence aux figures annexées suivantes :  The invention will be better understood on reading the description which follows, given with reference to the following appended figures:
- la figure 1 qui montre schématiquement en coupe longitudinale un premier exemple de mise en œuvre de l'invention ;  - Figure 1 which shows schematically in longitudinal section a first example of implementation of the invention;
- la figure 2 qui montre schématiquement en coupe longitudinale un deuxième exemple de mise en œuvre de l'invention.  - Figure 2 which shows schematically in longitudinal section a second example of implementation of the invention.
Sur la figure 1 , on a représenté une paroi métallique 1 appartenant à une installation implantée dans un milieu marin 2, telle qu'une plate-forme pétrolière ou une éolienne. Mais cette paroi 1 pourrait aussi être la coque d'un bateau, ou de tout autre engin navigant. De manière connue, une anode sacrificielle 3 est disposée au voisinage de la paroi 1 , à laquelle elle est reliée par des connecteurs électriques 4, 5. En général, comme dans l'art antérieur, l'anode sacrificielle 3 est réalisée autour d'un connecteur en acier unique, et dans ce cas, les connecteurs 4, 5 représentés sont en fait les deux extrémités de ce connecteur unique. Le matériau constitutif de l'anode sacrificielle 3 est classique à cet effet (Al-ln, Al-Ga ou alliage de Zn par exemple), et son choix n'est pas une caractéristique de l'invention. Selon l'invention, l'anode sacrificielle 3 est incluse dans un compartiment 6 qui est délimité par un ensemble de membranes formant des couches, et entoure l'anode 3 à une distance, par exemple, de l'ordre de 1 cm. In Figure 1, there is shown a metal wall 1 belonging to an installation located in a marine environment 2, such as an oil rig or a wind turbine. But this wall 1 could also be the hull of a boat, or any other flying craft. In known manner, a sacrificial anode 3 is disposed in the vicinity of the wall 1, to which it is connected by electrical connectors 4, 5. In general, as in the prior art, the sacrificial anode 3 is made around a single steel connector, and in this case, the connectors 4, 5 shown are in fact the two ends of this single connector. The constituent material of the sacrificial anode 3 is conventional for this purpose (Al-In, Al-Ga or Zn alloy for example), and its choice is not a characteristic of the invention. According to the invention, the sacrificial anode 3 is included in a compartment 6 which is delimited by a set of membrane forming layers, and surrounds the anode 3 at a distance, for example, of the order of 1 cm.
La couche la plus extérieure 7 est une couche poreuse perméable aux électrons et, de préférence, aussi à l'eau, destinée à réduire le flux hydraulique entre le milieu extérieur et l'espace intérieur 8 du compartiment. Le matériau qui la constitue est sélectionné parmi des matériaux polymères, des matériaux céramiques ou des matériaux inorganiques hydratés.  The outermost layer 7 is a porous electron-permeable layer and, preferably, also water, intended to reduce the hydraulic flow between the external environment and the interior space 8 of the compartment. The material constituting it is selected from polymeric materials, ceramic materials or hydrated inorganic materials.
Comme exemples de tels matériaux on peut citer, non limitativement, des polymères thermoplastiques du type polyéthylène ou polyéthylène haute densité, ou des porcelaines de type mullite ou alumine industrielles.  Examples of such materials include, but are not limited to, thermoplastic polymers of the polyethylene or high density polyethylene type, or industrial mullite or alumina type porcelains.
Si ce matériau est isolant électriquement, il doit présenter une porosité. En effet, la polarisation de l'anode correspond à l'établissement d'un petit circuit électrochimique, qui ne peut fonctionner que si les électrons circulent. La porosité ouverte permet aux électrons de passer dans le liquide même si la couche 7 est isolante.  If this material is electrically insulating, it must have porosity. Indeed, the polarization of the anode corresponds to the establishment of a small electrochemical circuit, which can only work if the electrons circulate. The open porosity allows the electrons to pass into the liquid even though the layer 7 is insulating.
Cette couche la plus extérieure 7, dont l'épaisseur est généralement de l'ordre du mm, a pour fonction de protéger l'anode et les autres membranes du compartiment 6 contre l'abrasion hydraulique. Elle doit présenter des propriétés adaptées de résistance à l'usure et aux impacts, de résistance à la déformation en présence d'un fluide en mouvement.  This outermost layer 7, whose thickness is generally of the order of mm, serves to protect the anode and the other membranes of the compartment 6 against hydraulic abrasion. It must have suitable properties of resistance to wear and impacts, resistance to deformation in the presence of a fluid in motion.
La perméabilité de la couche 7 est, par exemple, de l'ordre de 10 ml/min pour 1 cm2 de surface d'anode. The permeability of the layer 7 is, for example, of the order of 10 ml / min for 1 cm 2 of anode surface.
La ou les autres couches de la paroi du compartiment 6 (il y en a deux, 9, 10, dans l'exemple représenté) est ou sont constituées par un ou des matériaux servant de pièges à cations, et qui captent les cations émis par l'anode sacrificielle 3 pour éviter qu'ils ne se retrouvent dans le milieu marin 2. A cet effet, divers types de matériaux peuvent convenir : des membranes osmotiques, du charbon actif en poudre ou en granulés, une résine échangeuse de cations telle qu'une zéolite, un polymère capteur de cations à nanocharges négatives attirant les cations, des composés minéraux capteurs de cations tels que les phyllosilicates et les inosilicates. De tels matériaux figurent parmi ceux couramment utilisés en traitement et adoucissement de l'eau pour piéger ou échanger des cations. On peut leur ajouter une membrane en alumine activée ou en un composé fonctionnellement équivalent, qui, quant à elle, piège les contaminants chargés négativement, comme As et les fluorures, qui pourraient diminuer l'efficacité des membranes piégeant les cations. Des membranes semi-perméables mises en œuvre dans des procédés électrolytiques d'échange d'ions sont également utilisables. The other layer or layers of the wall of the compartment 6 (there are two, 9, 10, in the example shown) is or consist of one or more materials serving as cation traps, and which capture the cations emitted by the sacrificial anode 3 to prevent them from being found in the marine environment 2. For this purpose, various types of materials may be suitable: osmotic membranes, activated carbon powder or granules, a cation exchange resin such as a zeolite, a cation-attracting negative nanocharging cationic polymer, mineral cation-capturing compounds such as phyllosilicates and inosilicates. Such materials are among those commonly used in treating and softening water to trap or exchange cations. An activated alumina membrane or a functionally equivalent compound can be added to them, which in turn traps negatively charged contaminants, such as As and fluorides, that could decrease the efficiency of cation-trapping membranes. Semipermeable membranes used in electrolytic ion exchange processes can also be used.
Des membranes microporeuses organiques semi-perméables de nanofiltration d'un type retenant les cations peuvent aussi convenir.  Microporous organic semi-permeable nanofiltration membranes of a cation-retaining type may also be suitable.
Le nombre de couches de matériaux capteurs de cations peut être quelconque, au choix de l'utilisateur. Ces couches peuvent avantageusement être de multiples natures, chaque espèce de couche pouvant, par exemple, absorber de manière privilégiée une ou plusieurs des espèces chimiques que l'anode sacrificielle 3 est susceptible de libérer.  The number of layers of cation sensor materials can be arbitrary, at the user's choice. These layers may advantageously be of multiple natures, each layer species being able, for example, to preferentially absorb one or more of the chemical species that the sacrificial anode 3 is capable of releasing.
Par exemple, on peut prévoir :  For example, we can provide:
- une couche externe 9 perméable aux éléments chimiques de rayon inférieur à an outer layer 9 permeable to chemical elements with a radius less than
1 ,5 À et imperméable aux éléments chimiques de rayon supérieur à 1 ,5 À tels que Ca, K, Mg, Na ; 1, 5A and impervious to chemical elements of radius greater than 1.5A such as Ca, K, Mg, Na;
- et une couche interne 10 perméable aux éléments chimiques de rayon inférieur à 1 ,1 À tels que O, Cl, N (qui vont donc pouvoir pénétrer dans l'espace intérieur 8 du compartiment 6 ou en sortir, ce qui ne présente pas d'inconvénients), et imperméable aux éléments chimiques de rayon supérieur à 1 ,1 À tels que Al, Zn, Ga, In, donc les principaux éléments que peut émettre l'anode 3 sous forme de cations, et dont on ne souhaite pas qu'ils soient libérés dans le milieu environnant ; l'épaisseur des couches, notamment de la couche 10, peut varier de environ 1 mm à quelques cm, en fonction de la taille de l'anode 3 et, donc, de la quantité de cations à piéger.  and an inner layer 10 permeable to chemical elements with a radius of less than 1, 1 Å such that O, Cl, N (which will therefore be able to enter the internal space 8 of the compartment 6 or leave it, which does not present disadvantages), and impermeable to chemical elements of radius greater than 1, 1A such that Al, Zn, Ga, In, thus the main elements that can emit the anode 3 in the form of cations, and of which it is not desired that they are released into the surrounding environment; the thickness of the layers, in particular of the layer 10, can vary from about 1 mm to a few cm, depending on the size of the anode 3 and, therefore, the amount of cations to trap.
Dans le cas où l'ensemble de la paroi délimitant le compartiment 6 est perméable à l'eau, l'eau pénètre à l'intérieur du compartiment 6 et un équilibre des pressions est atteint entre l'intérieur et l'extérieur du compartiment 6. Le compartiment 6 prend donc en permanence sa forme nominale et sa paroi ne subit pas d'écrasement qui pourrait conduire à sa rupture.  In the case where the entire wall defining the compartment 6 is permeable to water, the water penetrates inside the compartment 6 and a pressure balance is reached between the inside and the outside of the compartment 6 The compartment 6 thus permanently takes its nominal form and its wall does not undergo crushing which could lead to its rupture.
Comme on l'a dit, il n'est pas obligatoire que l'ensemble de la paroi définissant le compartiment 6 soit perméable à l'eau. Elle peut n'être perméable qu'aux électrons, mais alors un pré-remplissage du compartiment 6 par de l'eau, de préférence de l'eau de mer, est nécessaire lors de la mise en service du dispositif selon l'invention.  As has been said, it is not mandatory that the entire wall defining the compartment 6 is permeable to water. It may be permeable only to electrons, but then pre-filling compartment 6 with water, preferably seawater, is necessary during commissioning of the device according to the invention.
Grâce à l'invention, la dissolution progressive de l'anode sacrificielle 3 s'effectue sans pollution du milieu extérieur par les cations résultant de cette dissolution, ceux-ci étant captés par la ou les couches 9, 10. Celles-ci doivent avoir avantageusement une capacité totale d'absorption des divers cations et un volume d'absorption suffisants pour ne pas parvenir à saturation avant la fin de vie de l'anode sacrificielle 3.  Thanks to the invention, the progressive dissolution of the sacrificial anode 3 is carried out without pollution of the external medium by the cations resulting from this dissolution, these being captured by the layer or layers 9, 10. These must have advantageously a total absorption capacity of the various cations and an absorption volume sufficient to not reach saturation before the end of life of the sacrificial anode 3.
Dans l'exemple représenté sur la figure 1 , les conducteurs électriques 4, 5 sont au contact de la paroi métallique 1 dans des zones situées hors du compartiment 6. Il faut donc assurer une étanchéité de la paroi du compartiment 6 dans les zones où elle est traversée par les conducteurs 4, 5. Mais en variante, comme représenté sur la figure 2, les contacts entre les conducteurs 5, 6 et la paroi métallique 1 peuvent être situés à l'intérieur du compartiment 6. La paroi du compartiment 6 est alors en contact étanche avec la paroi métallique 1 à protéger. In the example shown in Figure 1, the electrical conductors 4, 5 are in contact with the metal wall 1 in areas outside the compartment 6. It is necessary to therefore ensure a sealing of the wall of the compartment 6 in the areas where it is crossed by the conductors 4, 5. But alternatively, as shown in Figure 2, the contacts between the conductors 5, 6 and the metal wall 1 may be located inside the compartment 6. The wall of the compartment 6 is then in sealing contact with the metal wall 1 to be protected.
Comme représenté sur les figures, il est préférable que l'anode sacrificielle 3 ne soit pas au contact direct de la paroi 1 à protéger. On évite ainsi de créer des courts- circuits entre l'anode 3 et au moins la zone de la paroi 1 qui est en regard d'elle. De cette façon, une plus grande partie de la surface de la paroi 1 peut être protégée dans les meilleures conditions par une même anode 3. Des moyens de maintien de l'anode 3 à distance de la paroi 1 sont donc prévus, de préférence (non représentés sur les figures). Mais dans la pratique, ils pourront souvent être constitués par les connecteurs 4, 5, qui sont généralement en acier et présentent du fait de leur matériau et de leurs dimensions, une rigidité suffisante pour réaliser le maintien de l'anode 3 à distance de la paroi 1 .  As shown in the figures, it is preferable that the sacrificial anode 3 is not in direct contact with the wall 1 to be protected. This avoids creating short circuits between the anode 3 and at least the area of the wall 1 which is opposite it. In this way, a greater part of the surface of the wall 1 can be protected under the best conditions by the same anode 3. Means for holding the anode 3 away from the wall 1 are therefore provided, preferably ( not shown in the figures). But in practice, they can often be constituted by the connectors 4, 5, which are generally made of steel and have due to their material and their dimensions, a sufficient rigidity to achieve the maintenance of the anode 3 at a distance from the wall 1.
En variante, l'invention est aussi applicable au cas où l'anode n'est pas une anode sacrificielle au sens où elle a naturellement un potentiel électrochimique plus élevé que celui de la paroi 1 à protéger, mais est placée à ce potentiel par un générateur de courant continu ou redressé auquel elle est connectée par des conducteurs qui traversent la paroi du compartiment 6 de manière étanche.  In a variant, the invention is also applicable in the case where the anode is not a sacrificial anode in the sense that it naturally has a higher electrochemical potential than that of the wall 1 to be protected, but is placed at this potential by a DC or rectified current generator to which it is connected by conductors which pass through the wall of the compartment 6 sealingly.

Claims

REVENDICATIONS
1 . - Dispositif de protection cathodique d'une paroi métallique (1 ) contre la corrosion dans un milieu salin, comportant une anode et des moyens de connexion (4, 5) de ladite anode à ladite paroi (1 ), ladite anode étant à un potentiel électrochimique plus élevé que ladite paroi (1 ), caractérisé en ce que ladite anode est placée dans un compartiment (6) délimité par une paroi perméable aux électrons et, éventuellement, à l'eau, comportant : 1. - Device for cathodic protection of a metal wall (1) against corrosion in a salt medium, comprising an anode and connection means (4, 5) of said anode to said wall (1), said anode being at a potential electrochemical higher than said wall (1), characterized in that said anode is placed in a compartment (6) delimited by an electron-permeable wall and, optionally, water, comprising:
- une couche extérieure (7) poreuse en un matériau choisi parmi : des matériaux polymères, des matériaux céramiques ou des matériaux inorganiques hydratés ;  a porous outer layer (7) of a material chosen from: polymeric materials, ceramic materials or hydrated inorganic materials;
- et au moins une couche (9, 10) poreuse ayant la capacité de capter les cations émis par l'anode lors de sa dissolution, le matériau constituant ladite au moins une couche étant choisi parmi des membranes osmotiques, du charbon actif, une résine échangeuse de cations telle qu'une zéolite, un polymère capteur de cations à nanocharges, des composés minéraux capteurs de cations tels que des phyllosilicates et des inosilicates, des membranes microporeuses organiques semi-perméables de nanofiltration d'un type retenant les cations.  and at least one porous layer (9, 10) having the capacity of capturing the cations emitted by the anode during its dissolution, the material constituting said at least one layer being chosen from osmotic membranes, activated carbon, a resin cation exchanger such as a zeolite, a nano-cations cation-capturing polymer, mineral cation-capturing compounds such as phyllosilicates and inosilicates, microporous organic semi-permeable nanofiltration membranes of a cation-retaining type.
2. - Dispositif selon la revendication 1 , caractérisé en ce que ladite paroi (1 ) comporte également une membrane piégeant les contaminants chargés négativement.  2. - Device according to claim 1, characterized in that said wall (1) also comprises a membrane trapping negatively charged contaminants.
3.- Dispositif selon la revendication 1 ou 2, caractérisé en ce que l'anode est une anode sacrificielle (3) dont le potentiel électrochimique est naturellement supérieur à celui de la paroi métallique (1 ).  3.- Device according to claim 1 or 2, characterized in that the anode is a sacrificial anode (3) whose electrochemical potential is naturally greater than that of the metal wall (1).
4. - Dispositif selon la revendication 1 ou 2, caractérisé en ce qu'il comporte des moyens pour imposer à l'anode un potentiel électrochimique supérieur à celui de la paroi métallique (1 ).  4. - Device according to claim 1 or 2, characterized in that it comprises means for imposing on the anode an electrochemical potential greater than that of the metal wall (1).
5. - Dispositif selon l'une des revendications 1 à 4, caractérisé en ce que les moyens de connexion (4, 5) de l'anode à la paroi métallique (1 ) sont au contact de la paroi à l'extérieur du compartiment (6) et en ce qu'ils traversent de façon étanche la paroi poreuse du compartiment (6).  5. - Device according to one of claims 1 to 4, characterized in that the connecting means (4, 5) of the anode to the metal wall (1) are in contact with the wall outside the compartment (6) and in that they pass through the porous wall of the compartment (6).
6.- Dispositif selon l'une des revendications 1 à 4, caractérisé en ce que les moyens de connexion (4, 5) de l'anode à la paroi métallique (1 ) sont au contact de la paroi métallique (1 ) à l'intérieur du compartiment (6), et en ce que la paroi poreuse du compartiment (6) est connectée de manière étanche à la paroi métallique (1 ).  6.- Device according to one of claims 1 to 4, characterized in that the connection means (4, 5) of the anode to the metal wall (1) are in contact with the metal wall (1) to the inside the compartment (6), and in that the porous wall of the compartment (6) is sealingly connected to the metal wall (1).
7.- Dispositif selon l'une des revendications 1 à 6, caractérisé en ce qu'il comporte des moyens pour maintenir l'anode à distance de la paroi métallique (1 ). 7.- Device according to one of claims 1 to 6, characterized in that it comprises means for holding the anode away from the metal wall (1).
8.- Dispositif selon l'une des revendications 1 à 7, caractérisé en ce qu'il comporte une pluralité de couches (9,10) ayant la capacité de capter les cations émis par l'anode lors de sa dissolution, chaque couche (9, 10) captant de façon privilégiée des cations différents de ceux captés de façon privilégiée par les autres couches. 8.- Device according to one of claims 1 to 7, characterized in that it comprises a plurality of layers (9,10) having the ability to capture the cations emitted by the anode during its dissolution, each layer ( 9, 10) preferentially capturing different cations from those picked in a privileged way by the other layers.
EP13705736.0A 2012-02-01 2013-01-31 Device for the cathodic protection of a metal wall against corrosion in a saline environment Withdrawn EP2809830A1 (en)

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FR1250946A FR2986241B1 (en) 2012-02-01 2012-02-01 DEVICE FOR THE CATHODIC PROTECTION OF A METALLIC WALL AGAINST CORROSION IN A SALINE MEDIUM
PCT/EP2013/051837 WO2013113777A1 (en) 2012-02-01 2013-01-31 Device for the cathodic protection of a metal wall against corrosion in a saline environment

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CN103643238B (en) * 2013-11-27 2016-01-06 中交天津港湾工程研究院有限公司 A kind ofly ensure the device that sacrificial anode normally runs
CN103668221A (en) * 2013-12-16 2014-03-26 国家电网公司 Transformer substation grounding grid corrosion prevention protection construction method
CN106992280A (en) * 2017-04-12 2017-07-28 北京新能源汽车股份有限公司 Battery system of electric automobile and electric automobile
US11053653B2 (en) * 2017-08-04 2021-07-06 Ørsted Wind Power A/S Cathodic protection for offshore wind turbine steel support structures
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US20140332373A1 (en) 2014-11-13
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