EP0722000A1 - Vorrichtung für den Korrosionschutz einer Wasseranlage - Google Patents
Vorrichtung für den Korrosionschutz einer Wasseranlage Download PDFInfo
- Publication number
- EP0722000A1 EP0722000A1 EP96610001A EP96610001A EP0722000A1 EP 0722000 A1 EP0722000 A1 EP 0722000A1 EP 96610001 A EP96610001 A EP 96610001A EP 96610001 A EP96610001 A EP 96610001A EP 0722000 A1 EP0722000 A1 EP 0722000A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- anode
- cathode
- container
- electrode
- sensitive metal
- 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.)
- Granted
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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
-
- 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
- C23F2213/30—Anodic or cathodic protection specially adapted for a specific object
- C23F2213/31—Immersed structures, e.g. submarine structures
Definitions
- the present invention relates to an apparatus for corrosion protection of a water system, for example a hot water system, a radiator system or a process water system.
- cathodic protection It is usual to corrosion protect for example a container or other elements in a water system by applying a negative voltage to the container and a positive voltage to an electrode present in the container. This form of protection is generally described as cathodic protection.
- cathodic protection has the drawback that the protecting effect only extends to a relatively small area around the electrode connected as an anode, which results in that the following piping system is not protected against corrosion.
- Such a method comprises the use of an electrolysis system, i.e. a system, where the anode material is of an alkaline sensitive metal, like aluminium.
- the alkaline sensitive metal is aluminium, it will dissolve by electrolysis as the aluminium ion Al 3+ in the acid environment around the anode.
- aluminium ions formed by the electrolysis will convert, influenced by hydroxide formed by the cathode, to negative aluminate ions (AlO 2 - or Al(OH) 4 - ), due to the fact that the pH-value of the consumption water normally is in the weak basic area between pH 7,5 and pH 8,5.
- the aluminium ions have to pass an isoelectric point around pH 6.
- aluminium has a low solubility and it is presumed that the large observed deposit of sediment by electrolysis is due to precipitation of aluminium.
- the deposit of silt also means that there is less aluminium, dissolved from the anode, available for corrosion protection of the water system. Furthermore, if the container comprise a heating element, deposit on the heating element will cause a poor heat transmission from the heating element to the water in the container. Consequently, it is necessary frequently to clean the container.
- the present invention provides a hitherto unknown principle for production of ions of alkaline sensitive metal, wherein the alkaline sensitive metal is connected neither as anode nor as cathode, as disclosed in the prior art.
- the object of the present invention is to provide an apparatus for corrosion protection of a water system with less formation of silt, said corrosion protection being more effective than for a conventional cathodic protection system or an electrolysis system.
- an apparatus for corrosion protection of a water system comprising a container, fully or partly flown through by water, connected as cathode and/or comprising at least one cathode, the apparatus being provided with at least one anode, wherein cathode and anode are connected to a direct current (DC) source, which apparatus is characterized in that at least one electrode, comprising alkaline sensitive metal and electrically isolated from the cathode and the anode connected to the DC source, is provided such that at least a part of the electric current, running in the water from the anode to the cathode, is forced through the electrode comprising alkaline sensitive metal.
- DC direct current
- the side of the electrode comprising alkaline sensitive metal, facing the current running from the anode, will receive electrones. This will cause that there on this side will be a cathode reduction of the alkaline sensitive metal.
- the invention will in the following be exemplified with aluminium.
- the cathode reduction for aluminium is assumed to follow the following reaction equation: Al° + e - + 2H 2 O ⁇ AlO 2 - + 2H 2
- anode and cathode refer to electrodes connected as anode and cathode, respectively, i.e. connected to the positive and negative pole, respectively, on the DC source. These electrodes may both be of a permanent and/or a soluble type.
- a permanent electrode may be used an electrode comprising magnetite, platinized titanium, iron or graphite.
- a soluble electrode is preferred an electrode comprising one or more alkaline sensitive metals selected from aluminium, zinc, tin or lead, aluminium being preferred.
- a permanent electrode is used as an anode.
- the electrode comprising alkaline sensitive metal is selected such, that it comprises aluminium, zinc, tin, lead or mixtures thereof, preferably aluminium.
- the container which is connected as cathode and/or which comprises at least one cathode, such may be used, which is installed as a partial or a full stream container in the water system, or a container which of other reasons is installed in the water system, for example a hot water container or a pressure tank.
- the container may be of any suitable material, especially metal or metal alloys, for example metal material comprising iron. If the container is of a material, or the container is fully coated with a material, which is not electrical conducting, the container obligatory comprises one or more cathodes.
- the container when the container is connected as a cathode, is also meant, besides the container flown through by water, arrangements in the container electrically connected with the container, and thereby having the same potential.
- the at least one anode, provided in the apparatus may be present in the same container as the container connected as cathode and/or comprising at least one cathode, but the anode may also be present in a separate container, or in a separate chamber, which maybe is in liquid communication with the first mentioned container.
- electrical isolated alkaline sensitive metal may be placed between cathode and anode.
- electrical isolated alkaline sensitive metal may be placed between cathode and anode.
- the walls of the container may fully or partly be constituted of an electrically isolating material.
- this electrically isolating material is provided in areas, where an electrically isolating alkaline sensitive metal is not placed between the at least one anode and a container wall used as cathode.
- a way to obtain a better control of the currents is to separate the at least one anode from the at least one cathode present in the same container by providing two chambers, which might be in liquid communication. This may for example be provided by partition in the container separating anodes from cathodes.
- a first chamber comprises at least one cathode and at least one electrode, isolated from the cathode, which might comprise alkaline sensitive metal
- a second chamber comprises at least one anode and at least one electrode, isolated from the anode, comprising alkaline sensitive metal, the electrodes isolated from anode and cathode in the two chambers being connected, thereby obtaining the same potential.
- Another way to obtain a better control of the currents is to separate the at least one anode from the at least one cathode in separate containers.
- a first container is connected as cathode and/or comprises at least one cathode and comprises at least one electrode electrically isolated from the cathode
- a second container comprises at least one anode and at least one electrode electrically isolated from the anode, comprising alkaline sensitive metal, the electrodes isolated from anode and cathode in the two containers being connected, thereby obtaining the same potential.
- the measured current is a direct expression for the amount of dissolved alkaline sensitive metal and it is therefore possible to control the formation of ions of alkaline sensitive metal by changing the amount of current supplied to anode and cathode from the DC source, so that the corrosion protection at any time can operate optimally, even under changed conditions, such as a changed amount of flowing water in the water system, a changed water temperature, a changed pH-value of the water, etc.
- An essential advantage by using an apparatus according to the invention with separate chambers or containers is that different ions of alkaline sensitive metal in the two chambers/containers are formed, when electrodes of alkaline sensitive metal isolated from cathode and anode, are used in both containers.
- the chamber/container comprising the at least one cathode the positive ion is produced
- the chamber/container comprising the at least one anode the negative ion is produced. If, for example, only the negative ion is desired, one may omit to connect the chamber/container comprising the cathode to the same water system as the chamber/container comprising the anode.
- a permanent electrode in the chamber/container comprising the cathode which permanent electrode is isolated from the cathode but is connected to the electrode comprising alkaline sensitive metal in the chamber/container comprising the at least one anode. If aluminium is used as alkaline sensitive metal, then it is possible to supply the water system with the desired aluminate ion.
- the inner walls of these containers are preferably coated with, or the containers mainly consists of, electrical isolating material.
- the cathode and the anode, respectively may favourably be placed close to or embedded in the wall of electrical isolating material and the electrodes isolated from cathode and anode may be provided in the centre of the container with free liquid flow to all sides.
- the apparatus such in the water system that a constant part of the full flow passes through the apparatus. This is, in general, ensured by connecting a feeding pump, which supply a constant flow rate. If desired, the amount of current, which is supplied to the anodes and the cathodes, is adjusted dependent on the full flow, so that ions of alkaline sensitive metal are released in dependence on the consumed amount of water.
- the electrode isolated from the cathode in the cathode container receives the total applied amount of current (calculated in Coulomb), which is applied to the anode and the isolated electrode in the anode container.
- This method has been proven effective to remove even hard coatings on the cathode, and it may be used in combination with alternating polarity.
- a cathodic protected hot water container is used as a first container connected as cathode, i.e. a hot water container is used, which is connected as cathode and which is provided with at least one anode.
- a second container such is used which on the inner walls is coated with, or mainly consist of, an electrical isolating material and which comprises at least one anode placed, relative to at least one electrode comprising alkaline sensitive metal and isolated from the anode, such that at least a part of the water flowing through the container passes between, the electrodes in the hot water container and the electrical isolated electrodes in the other container electrically being connected.
- the electrode in the hot water container can either be soluble, i.e. comprise alkaline sensitive metal, preferably aluminium, or insoluble. If the electrode is soluble, positive ions of alkaline sensitive metal are released, which locally, in the hot water container, have a possible corrosion protecting effect. If the electrode is permanent the well-known cathodic protection is obtained.
- the advantage of the above mentioned embodiment of the apparatus according to the invention is primarily, that the same electrical circuit may be used both to corrosion protection of a hot water container in a water system and for corrosion protection of the following water system by production of the negative ions of alkaline sensitive metal suited for this purpose. Further, a large number of existing water systems comprising a cathodic protected hot water container can be upgraded by either the mounting of another container of the above mentioned type on the hot water container, or by providing such further container in the following water system.
- formation of deposits may appear in the other container comprising the at least one anode.
- the electrode operating as anode in one time period changes polarity to cathode in another time period.
- the cathodic potential of the hot water container, and the potential of the at least one electrode in the hot water container is maintained constant during the changing polarity of the anode to avoid corrosion of the hot water container.
- the present invention also relates to an apparatus part for corrosion protection of a water system, which apparatus part comprises a container, fully or partly flown through by the water, comprising at least one anode connected to a DC source, which apparatus part being characterized in that at least one electrode, comprising alkaline sensitive metal and electrically isolated from the anode connected to the DC source, is provided such that at least a part of the electrical current running in the water from the anode to an external cathode, is forced through the electrode comprising alkaline sensitive metal.
- the water is introduced into a container 1 through an opening 2.
- the container comprises a permanent anode 3 and two electrodes 4 comprising alkaline sensitive metal, especially aluminium.
- the electrodes 4 are electrically isolated from the container with an insulating material 6.
- the water is discharged through an outlet 5.
- the container 1 is electrically connected as cathode, and the anode 3 is connected as anode.
- the current direction is illustrated by arrows, which passes from the anode through the alkaline sensitive metal to the cathode.
- Fig. 2 the apparatus from Fig. 1 is disclosed from above.
- two of the walls in the container is provided with an electrically isolating material 7.
- Fig. 3 discloses an embodiment according to the invention, where a device is inserted in an existing container.
- the device is of two pieces of flat bar 9, which is welded on the inner wall of the container 1, wherein aluminium material, anode and aluminium material are placed in the successive order between the two pieces of flat bar 9 .
- the two pieces of aluminium material are electrically isolated from both cathode and anode of an electrically isolating plate 8, onto which they are installed.
- Fig. 4 discloses a possible placing of the devices shown in Fig. 3 in a hot water container.
- Fig. 5 discloses an apparatus, where the water is introduced into a container 1 through the opening 2.
- the container consists of a insulating material.
- the container comprises an aluminium electrode 4 placed between a permanent anode 3 and a permanent cathode 10.
- the electrode 4 is electrically isolated from the container with an insulating material 6.
- the anode 3 and the cathode 10 is connected to a DC source.
- FIG. 6 the apparatus from Fig. 5 is disclosed in a horizontal cross-sectional view.
- Fig. 7 discloses an apparatus, where a container 1 is separated by a partition wall 11 in a cathode chamber 12 and an anode chamber 13.
- the cathode chamber 12 is provided with a spiral-shaped cathode 10 connected to a negative pole on a not shown DC source.
- the cathode 10 is placed around an aluminium electrode 4 without coming into contact with it and the aluminium electrode is isolated from the container by an insulating material 6.
- the anode chamber is constructed in the same way as the cathode chamber, an anode 3 being provided instead of a cathode.
- the two aluminium electrodes 4 in the anode chamber and in the cathode chamber are electrically connected.
- the polarity may, if desired, be alternated constantly or according to requirement, so the electrodes functioning as anode and cathode, respectively, in one time period change polarity to cathode and anode, respectively, in another time period. Furthermore, it might be desirable constantly or according to requirement, possibly in combination with operating with alternating polarity, to apply a positive voltage to the aluminium electrodes 4 to prevent or eliminate coatings.
- Fig. 7 the partition wall is provided such that the two chambers are in liquid communication.
- this is no condition, as ions of aluminium independently are produced in the individual chambers, which means that the individual chambers may be connected with separate water systems or the same water system in different areas.
- Fig. 8 discloses an apparatus separated in two containers, a cathode container 14 and an anode container 15.
- the cathode container 14 is provided with a spiral-shaped cathode 10 connected with a negative pole on a not shown DC source.
- the cathode 10 is placed around an aluminium electrode 4 without coming into contact with it, and the aluminium electrode is isolated from the cathode container 14 by a insulating material 6.
- the anode container 15 is constructed in the same way as the cathode container, an anode 3 being provided instead of a cathode.
- the two aluminium electrodes in the anode container and cathode container are electrically connected.
- the polarity may, if desired be alternated constantly or according to requirement, so the electrodes functioning as anode and cathode, respectively, in one time period may change polarity to cathode and anode, respectively, in another time period. Furthermore, it might be desirable constantly or according to requirement, possibly in combination with operating with alternating polarity, to apply a positive voltage to the aluminium electrodes 4 to prevent or eliminate coatings.
- Fig. 8 the two containers are shown as being in liquid communication. However, this is no condition, as ions of aluminium independently are produced in the individual containers, which means that the individual containers may be connected with separate water systems or the same water system in different areas.
- a hot water container 17 is used as cathode, as the hot water container 17 is connected with the negative pole on a DC source.
- an anode container 15 comprising a spiral-shaped anode 3 connected with the positive pole on a DC source, is provided, the anode being placed around an aluminium electrode 4 isolated from the anode container 15 by a insulating material 6.
- the aluminium electrode 4 is electrically connected with another aluminium electrode 16 placed in the hot water container 17.
- the anode container is supplied with a constant flow rate by the pump 18.
- aluminate ions for protection of the water system, are produced and in the hot water container positive aluminium ions are produced, which are presumed to be inhibitors to local corrosion of the hot water container. If the presence of a soluble aluminium electrode in the container causes a too big siltation, a insoluble electrode may alternatively be used.
- the polarity of the anode may, if desired, be change, if a formation of coating occur. Such change of the polarity may for example be periodic or may be carried out according to requirement. If an alternation of the polarity of the anode is carried out, the anode container on the inside has to be coated with, or mainly consists of, an electrically inert material, i.e. an electrically isolating material to avoid corrosion of the container.
- an electrically inert material i.e. an electrically isolating material to avoid corrosion of the container.
- Fig. 10 discloses an embodiment, where an anode container 15 has been mounted on an existing cathodicly protected hot water container 17 in a water system.
- An aluminium electrode 4 in the anode container is electrically connected with a permanent electrode 19, which hereby obtains the capability as an anode.
- the water system is supplied with aluminate ions from the anode container, at the same time as the hot water container continuously is protected against corrosion.
- the polarity of the anode may, if desired, be alternated. However, it has to be ensured that the hot water container at the same time remains cathodicly protected.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK96610001T DK0722000T4 (da) | 1995-01-13 | 1996-01-10 | Apparat til korrosionsbeskyttelse af et vandsystem |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK3595 | 1995-01-13 | ||
DK35/95 | 1995-01-13 | ||
DK3595 | 1995-01-13 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0722000A1 true EP0722000A1 (de) | 1996-07-17 |
EP0722000B1 EP0722000B1 (de) | 1998-04-01 |
EP0722000B2 EP0722000B2 (de) | 2004-04-14 |
Family
ID=8089008
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96610001A Expired - Lifetime EP0722000B2 (de) | 1995-01-13 | 1996-01-10 | Vorrichtung für den Korrosionschutz einer Wasseranlage |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0722000B2 (de) |
AT (1) | ATE164637T1 (de) |
DE (1) | DE69600203T3 (de) |
DK (1) | DK0722000T4 (de) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1418867A (fr) * | 1964-06-29 | 1965-11-26 | Procédé et dispositif de protection contre la corrosion et la salissure de structures métalliques immergées par génération électrolytique, sans diaphragme, d'ionsferreux | |
DE2445903A1 (de) * | 1974-09-26 | 1975-11-13 | ||
WO1991014018A1 (en) * | 1990-03-12 | 1991-09-19 | I. Krüger As | Electrolytic apparatus for protection against corrosion of a freshwater piping system |
US5344537A (en) * | 1990-09-27 | 1994-09-06 | Guldager Electrolyse A/S | Method for corrosion-proofing of a water system |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62210096A (ja) † | 1986-01-21 | 1987-09-16 | ウイルフレツド・アンソニ−・マ−レル | 水処理方法及び水処理装置 |
-
1996
- 1996-01-10 DE DE69600203T patent/DE69600203T3/de not_active Expired - Fee Related
- 1996-01-10 EP EP96610001A patent/EP0722000B2/de not_active Expired - Lifetime
- 1996-01-10 DK DK96610001T patent/DK0722000T4/da active
- 1996-01-10 AT AT96610001T patent/ATE164637T1/de not_active IP Right Cessation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1418867A (fr) * | 1964-06-29 | 1965-11-26 | Procédé et dispositif de protection contre la corrosion et la salissure de structures métalliques immergées par génération électrolytique, sans diaphragme, d'ionsferreux | |
DE2445903A1 (de) * | 1974-09-26 | 1975-11-13 | ||
WO1991014018A1 (en) * | 1990-03-12 | 1991-09-19 | I. Krüger As | Electrolytic apparatus for protection against corrosion of a freshwater piping system |
US5344537A (en) * | 1990-09-27 | 1994-09-06 | Guldager Electrolyse A/S | Method for corrosion-proofing of a water system |
Also Published As
Publication number | Publication date |
---|---|
EP0722000B1 (de) | 1998-04-01 |
DK0722000T3 (da) | 1998-11-30 |
DE69600203T2 (de) | 1998-10-22 |
DE69600203T3 (de) | 2004-12-30 |
EP0722000B2 (de) | 2004-04-14 |
DK0722000T4 (da) | 2004-05-10 |
DE69600203D1 (de) | 1998-05-07 |
ATE164637T1 (de) | 1998-04-15 |
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