GB2351739A - Electrode containing an electrical conductor connected inside - Google Patents

Electrode containing an electrical conductor connected inside Download PDF

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Publication number
GB2351739A
GB2351739A GB9917015A GB9917015A GB2351739A GB 2351739 A GB2351739 A GB 2351739A GB 9917015 A GB9917015 A GB 9917015A GB 9917015 A GB9917015 A GB 9917015A GB 2351739 A GB2351739 A GB 2351739A
Authority
GB
United Kingdom
Prior art keywords
electrode
electrode according
electrical conductor
spaced apart
liquid
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
Application number
GB9917015A
Other versions
GB9917015D0 (en
GB2351739B (en
Inventor
Andrew Hill
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.)
Atraverda Ltd
Original Assignee
Atraverda Ltd
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 Atraverda Ltd filed Critical Atraverda Ltd
Publication of GB9917015D0 publication Critical patent/GB9917015D0/en
Priority to US10/019,606 priority Critical patent/US6998031B1/en
Priority to PCT/GB2000/002553 priority patent/WO2001002626A1/en
Priority to CN00809912A priority patent/CN1359431A/en
Priority to AT00944100T priority patent/ATE309398T1/en
Priority to EP00944100A priority patent/EP1409768B1/en
Priority to DE60023958T priority patent/DE60023958T2/en
Priority to JP2001508395A priority patent/JP4658421B2/en
Priority to CN2007100917608A priority patent/CN101135057B/en
Priority to AU58336/00A priority patent/AU773688B2/en
Priority to DK00944100T priority patent/DK1409768T3/en
Priority to ES00944100T priority patent/ES2250153T3/en
Priority to CA002377796A priority patent/CA2377796C/en
Publication of GB2351739A publication Critical patent/GB2351739A/en
Application granted granted Critical
Publication of GB2351739B publication Critical patent/GB2351739B/en
Priority to HK08109612A priority patent/HK1120294A1/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09CRECLAMATION OF CONTAMINATED SOIL
    • B09C1/00Reclamation of contaminated soil
    • B09C1/08Reclamation of contaminated soil chemically
    • B09C1/085Reclamation of contaminated soil chemically electrochemically, e.g. by electrokinetics
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46133Electrodes characterised by the material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46152Electrodes characterised by the shape or form
    • C02F2001/46157Perforated or foraminous electrodes
    • C02F2001/46161Porous electrodes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Soil Sciences (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

An electrode comprises an elongate tube made of titanium suboxide, the tube containing an electrical conductor in the form of a coil 11 in contact with the inside wall of the tube at spaced apart locations, the coil being connected to a power source. The electrical conductor may be a valve metal, eg titanium. The electrode may be used in the treatment of fluids, eg water, to remove pollutants therefrom.

Description

2351739 Aqent's Ref: P02653GB ELECTRODE The invention relates to an
electrode formed of low conductivity material. Typically such electrodes take the form of an elongate hollow body. Preferably the body is made of a substoichiometric oxide of titanium or the like in which case it is likely that the most effective manufacturing route will result in the body being porous.
It has been calculated, by way of illustration, based on a tubular body 500 mm long, 18 mm outside diameter with a 3 mm wall thickness, made of a material with a volume resistivity of 30 mO.cm, operating with an electrical connection at the one end, supplied with a current of 2.83 Amps (intended to provide a current density of 1 OOA/M2 at all points along its length) that there will be a voltage drop of about 750mV between the ends of such an electrode. In many electrochemical applications and as a result of this voltage drop there may be regions of the electrode where the potential is insufficient to perform its intended function. In the case of an electrolytic process operating at low voltages between anode and cathode (the preferred situation since this leads generally to lower electrical costs) of the order of I to 5V it cannot be guaranteed that all the surface area of the electrode Vill be equally effective, or effective at all. This is particularly true of electrolytic processes, such as water treatment, which are favoured by electrode surfaces which exhibit high gassing overpotential (such as titanium suboxides, lead dioxide, doped tin dioxide etc). In such cases, the actual current density can be shown to vary by more than 50% between the ends of such an electrode.
2 It is one object of this invention to provide a method of making an electrical connection to such an electrode which will solve this problem, particularly in the context of the electrode body being made of a porous material.
In one aspect the invention provides an electrode comprising an elongate generally hollow body formed of low electrical conductivity material, an electrical conductor being connected to a power source and located inside the body at spaced apart locations and arranged so that the current is distributed substantially uniformly along the electrode.
The conductor is made of a material with an electrical conductivity substantially higher (at least 2 orders of magnitude) than that of the electrode body. In one form the conductor is a coiled length of spring wire shaped so as to mechanically urge the coils into contact with the inner wall surface of the tubular body at regular intervals. In another embodiment separate conductor lengths are present at longitudinal spaced apart locations and each contacts the inner wall of the cylinder.
The body may be formed from a range of materials. Most preferably the electrode body is formed of a substoichiometric oxide of titanium of the form TiO, where x is from about 1.99 to about 1.7. Such a body is generally porous since the more most cost-effective manufacturing routes to a cylindrical or hollow body of such materials results in a porous structure. Catalytic elements may be present. In a preferred embodiment the electrode body is formed of the substoichiometric oxide of titanium and the electrode conductor is a valve metal, whereby a durable electrical connection is made.
The body is preferably at least 200 mm long when the invention is valuable for use with materials for which the volume resistivity is higher than about 20mQ.cm. If the 3 material of the body is of higher resistivity then the invention is valuable for use where the body is at least 150 mm long.
The electrode of the invention is useful in many processes where cylindrical electrode geometry is advantageous, such as in the treatment of fluids to remove pollutants, and in the in-situ remediation of contaminated soils. Generally, water pollutants can be grouped in seven classes as follows:
1. Sewage and other oxygen-demanding wastes 2. Infectious agents 3. Plant nutrients 4. Exotic organic chemicals 5. Inorganic minerals and chemical compounds 6. Sediments 7. Radioactive substances.
Sewage and other oxygen-demanding wastes are generally carbonaceous organic materials that can be oxidised biologically (or sometimes chemically) to carbon dioxide and water. These wastes can be problematic. Infectious agents are usually found in waste water from municipalities, sanatoriums, tanning and slaughtering plants and boats. This type of pollutant is capable of producing disease in man and animals, including livestock.
Plant nutrients, (e.g. nitrogen and phosphorus) are capable of stimulating the growth of aquatic plants which interfere with water usage and which later decay to produce annoying odours and increase the amount of oxygen-demanding waste in the water.
4 Exotic organic chemicals include surfactants used in detergents, pesticides, various industrial products and the decomposition products of other organic compounds. Some of these compounds are known to be toxic to fish at very low concentrations. Many of these compounds are not readily biologically degradable.
Inorganic minerals and chemical compounds are generally found in water from municipal and industrial waste waters and from urban run-off. These pollutants can kill or injure fish and other aquatic life and can also interfere with the suitability of water for drinking or industrial use. A prominent example is the occurrence of mercury in water. Another example is salt pollution used to de-ice roads in winter in the northern, colder climates.
Sediments are soil and mineral particles washed from the land by storms and floodwaters, from croplands, unprotected forest soils, overgrazed pastures, strip mines, roads and bulldozed urban areas. Sediments fill stream channels and reservoirs; erode power turbines and pumping equipment, reduce the amount of sunlight available to aquatic plants; plug water filters; and blanket fish nests, spawn and food supplies, thereby reducing the fish and shelf fish populations.
Radioactive substances in water environments usually result from the wastes of uranium and thorium mining and refining; from nuclear power plants and from industhal, medical, scientific utilisation of radioactive materials.
In another aspect the invention provides apparatus for use in electrolytic treating of a liquid comprising a chamber containing the fluid to be treated, an anode and a cathode at least one of which is an electrode as disclosed herein, and a supply of electrical current.
The invention is seen to particularly good effect in the treatment of water or aqueous media. In such a case electrical current is passed between an anode and a cathode across a small gap, through which the water is passed. Because of the structure of an electrode of the invention one can guarantee that a predetermined minimum voltage, e.g. 3V will be present along the length of the electrode.
Electrodes made of titanium suboxide has a high gassing overpotential, i. e. the voltage required before any appreciable current passes because of the low catalytic activity of the surface for splitting water into hydrogen and hydroxyl radicals. This level is in excess of 1V unless the surface is catalysed, so the effective driving force for current is at most about 2V (if the overall voltage is 3V as above) near the connector and 1.25 volts at the other end due to the voltage drop along the electrode in the absence of this invention, under the conditions described above.
In yet another aspect the invention provides a method of operating apparatus as disclosed herein, including supplying a current from the power source to the electrode of low conductivity at a current density of more than 10 A. M2 of external anode area, whereby the voltage variation between any two points on the electrode is less than 200 mV.
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 diagram showing a representative electrochemical cell for the treatment of water; Figure 2 is an enlarged view partly in section of one embodiment shown in the diagram of Figure 1 and Figure 3 is the same of another embodiment.
6 The water treatment system includes a cell whereby the water being treated is introduced to the annular space 2 between two elongate tubular bodied electrodes, with a small annular clearance in between. Each electrode is typically 500 mm long and is connected to the respective poles of a D.C. supply 4 so that one electrode is a cathode 5 and the other (in illustration, the inner electrode) an anode 6. The inner electrode is typically 18 mm outside diameter and the annular space is typically 2 mm. When current is passed through the electrodes an electrolytic reaction takes place, such as treating the water to remove pollutants. The water passes in the annular clearance between the electrodes. Typically the electrical connection is made to one end of the inner electrode and a current of about 2.83 amps is supplied. If the inner electrode is made of a titanium suboxide tube with a wall thickness of 3 mm and which has a volume resistivity of -30mQ.cm, a voltage drop of about 75OmV will occur down the length of the inner electrode in the absence of this invention, so that the cell potential at one end will be about 3V and at the other 2.25V.
According to the invention the anode 6 of Figure 1 comprises an elongate tube 10 formed of titanium suboxide by moulding, extrusion or the like. The tube is about 500 mm long, having an inner diameter of 12 mm and an outer diameter of 18 mm, i.e. a wall thickness of about 3 mm.
According to one embodiment of the invention and as shown in Figure 2, the current feeder comprises a length of titanium spring wire 11 which extends along the inner bore of the tube. One end of the wire 11 is connected to the power source 4, the other end may be sealed by an end cap. The coils of the spring are mechanically urged into contact with the inner wall of the tube at longitudinally spaced apart locations L whereby the supply is distributed substantially uniformly along the length of the tube. As a result the cell voltage is substantially the same along the entire 7 length of the cell and hence the entire length is effective in its electrochemical function, such a killing m icro-organ isms, oxidising and/or reducing contaminants.
The cathode may be the same shape as the anode or it may be of standard design.
In the embodiment shown in Figure 3, the coil spring is replaced by a series of individual connectors 12 spaced apart along the length of the tube.
The invention is not limited to the embodiment shown. The water treatment apparatus may comprise banks of cells, and include other treatments. The electrode need not be circular in section. Although the invention has been described in relation to water treatment, the electrode has value in any situation where an elongate electrode is useful. Such applications include in-situ soil remediation, and electrochemical synthesis reactions, e.g. a redox system.
8

Claims (14)

1. An electrode comprising an elongate generally hollow body formed of low electrical conductivity material, an electrical conductor being connected to a power source and located inside the body at spaced apart locations and arranged so that the current is distributed substantially uniformly along the electrode.
2. An electrode according to Claim 1, wherein the electrical conductor extends along substantially along the length of the body.
3. An electrode according to Claim 2, wherein the conductor is a coil length of spring wire shaped so as to mechanically urge the coils into contact with the inner wall surface of the body at longitudinally spaced apart locations.
4. An electrode according to any preceding Claim, wherein separate conductors are present at longitudinal spaced apart locations and each contacts the inner wall of the body.
5. An electrode according to any preceding Claim, wherein the electrode body is formed of a substoichiometric suboxide of titanium of the form TiQ, where x is from about 1.99 to about 1.7.
6. An electrode according to any preceding Claim, wherein the body is at least mm long.
7. An electrode according to any preceding Claim, wherein the electrical conductor is made of a valve metal.
9 8. Apparatus for use in electrolytic treatment of a liquid, the apparatus comprising a chamber containing the liquid to be treated, an anode and a cathode at least one of which is an electrode according to any of Claims 1 to 7.
g. Apparatus according to Claim 8, wherein the liquid is aqueous effluent or water and the treatment is to remove pollutants.
10. A method of operating apparatus according to Claim 8 or 9 including supplying a current from the power source to the electrode at a density of above 10 A. M2 of external anode area, whereby the voltage variation between any two points on the electrode is less than 200 mV.
11. An in-situ soil remediation system incorporating an electrode according to any of Claims 1 to 7.
12. Apparatus for performing a redox type reaction, incorporating an electrode according to any of Claims 1 to 7.
LSrjw/P026MB 16107199 0 'c:> Amendments to the claims have been filed as follows CLAIMS 1. An electrode comprising an elongate generally hollow body formed of low electrical conductivity material, and an electrical conductor in the form of an elongate spring member made of spring wire, said spring wire being located inside said body for portions of the spring wire to be urged by spring action into contact with the inner wall surface of the body at spaced apart locations along the length of the body, the electrical conductor being operable for being connected to a power source and for causing a resulting electrical current in the electrode to be distributed substantially uniformly along the electrode.
2. An electrode according to Claim 1, wherein the spring member extends along substantially the whole of the length of the body.
3. An electrode according to Claim 2, wherein the spring member is a coil spring.
4. An electrode according to any preceding Claim, wherein separate conductors are present at longitudinal spaced apart locations and each contacts the inner wall of the body.
5. An electrode according to any preceding Claim, wherein the electrode body is formed of a substoichiometric suboxide of titanium of the form TiO, where x is from about 1.99 to about 1.7.
6. An electrode according to any preceding Claim, wherein the body is at least mm long.
7. An electrode according to any preceding Claim, wherein the electrical conductor is made of a valve metal.
8. An electrode according to any of Claims 1 to 6, wherein the electrical conductor is made of titanium spring wire.
9. Apparatus for use in electrolytic treatment of a liquid, the apparatus comprising a chamber containing the liquid to be treated, an anode and a cathode at least one of which is an electrode according to any of Claims 1 to 8.
10. Apparatus according to Claim 9, wherein the liquid is aqueous effluent or water and the treatment is to remove pollutants.
11. A method of operating apparatus according to Claim 9 or 10 including supplying a current from the power source to the electrode at a density of above 10 A. M2 of external anode area, whereby the voltage variation between any two points on the electrode is less than 200 mV.
12. An in-situ soil remediation system incorporating an electrode according to any of Claims 1 to 8.
13. Apparatus for performing a redox type reaction, incorporating an electrode according to any of Claims 1 to 8.
14. An electrode substantially as hereinbefore described with reference to the accompanying drawings.
GB9917015A 1999-07-01 1999-07-20 Electrode Expired - Fee Related GB2351739B (en)

Priority Applications (13)

Application Number Priority Date Filing Date Title
US10/019,606 US6998031B1 (en) 1999-07-01 2000-03-07 Electrode
AT00944100T ATE309398T1 (en) 1999-07-01 2000-07-03 ELECTRODE
ES00944100T ES2250153T3 (en) 1999-07-01 2000-07-03 ELECTRODE.
PCT/GB2000/002553 WO2001002626A1 (en) 1999-07-01 2000-07-03 Electrode
EP00944100A EP1409768B1 (en) 1999-07-01 2000-07-03 Electrode
DE60023958T DE60023958T2 (en) 1999-07-01 2000-07-03 ELECTRODE
JP2001508395A JP4658421B2 (en) 1999-07-01 2000-07-03 electrode
CN2007100917608A CN101135057B (en) 1999-07-01 2000-07-03 Electrode
AU58336/00A AU773688B2 (en) 1999-07-01 2000-07-03 Electrode
DK00944100T DK1409768T3 (en) 1999-07-01 2000-07-03 electrode
CN00809912A CN1359431A (en) 1999-07-01 2000-07-03 Electrode
CA002377796A CA2377796C (en) 1999-07-01 2000-07-03 Electrode
HK08109612A HK1120294A1 (en) 1999-07-01 2008-08-29 Electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB9915420A GB9915420D0 (en) 1999-07-01 1999-07-01 Electrode

Publications (3)

Publication Number Publication Date
GB9917015D0 GB9917015D0 (en) 1999-09-22
GB2351739A true GB2351739A (en) 2001-01-10
GB2351739B GB2351739B (en) 2004-01-21

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Family Applications (2)

Application Number Title Priority Date Filing Date
GB9915420A Ceased GB9915420D0 (en) 1999-07-01 1999-07-01 Electrode
GB9917015A Expired - Fee Related GB2351739B (en) 1999-07-01 1999-07-20 Electrode

Family Applications Before (1)

Application Number Title Priority Date Filing Date
GB9915420A Ceased GB9915420D0 (en) 1999-07-01 1999-07-01 Electrode

Country Status (4)

Country Link
CN (1) CN101135057B (en)
GB (2) GB9915420D0 (en)
HK (1) HK1120294A1 (en)
RU (1) RU2247175C2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2511266C1 (en) * 2012-10-30 2014-04-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Челябинская государственная агроинженерная академия" Device for cleaning agricultural soil from pesticides

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103046071B (en) * 2012-12-13 2015-02-18 苏州市启扬商贸有限公司 Ion membrane electrolysis unit tank
RU2538106C2 (en) * 2013-03-04 2015-01-10 Юрий Константинович Курчаков Electrolyser-neutraliser of dissociated contaminations
CN104451795B (en) * 2014-10-23 2017-07-28 贵州红林机械有限公司 A kind of electrodeposited chromium device for step-like inner hole part
KR102272749B1 (en) * 2016-11-22 2021-07-06 아사히 가세이 가부시키가이샤 Electrode for electrolysis

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2863819A (en) * 1955-08-25 1958-12-09 Herman S Preiser Insoluble trailing anode for cathodic protection of ships
US4033849A (en) * 1975-05-09 1977-07-05 Diamond Shamrock Corporation Electrode and apparatus for forming the same
US4154667A (en) * 1978-01-03 1979-05-15 Diamond Shamrock Corporation Method of converting box anodes to expandable anodes
US4388162A (en) * 1982-02-08 1983-06-14 Institute Of Gas Technology Continuous flow electrochemical cell and process
US4486288A (en) * 1982-03-11 1984-12-04 Linder Bjoern H Oxide anode for use in impressed current cathodic corrosion protection
EP0224851A1 (en) * 1985-11-27 1987-06-10 Heraeus Elektroden GmbH Electrode for electrochemical processes
US4710644A (en) * 1985-10-30 1987-12-01 Corrpro Companies, Inc. Replaceable deep anode system
US4966675A (en) * 1988-03-15 1990-10-30 Steininger Karl Heinz Polarizable electrode
US5584975A (en) * 1995-06-15 1996-12-17 Eltech Systems Corporation Tubular electrode with removable conductive core
GB2309978A (en) * 1996-02-09 1997-08-13 Atraverda Ltd Titanium suboxide electrode; cathodic protection

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4422917A (en) * 1980-09-10 1983-12-27 Imi Marston Limited Electrode material, electrode and electrochemical cell

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2863819A (en) * 1955-08-25 1958-12-09 Herman S Preiser Insoluble trailing anode for cathodic protection of ships
US4033849A (en) * 1975-05-09 1977-07-05 Diamond Shamrock Corporation Electrode and apparatus for forming the same
US4154667A (en) * 1978-01-03 1979-05-15 Diamond Shamrock Corporation Method of converting box anodes to expandable anodes
US4388162A (en) * 1982-02-08 1983-06-14 Institute Of Gas Technology Continuous flow electrochemical cell and process
US4486288A (en) * 1982-03-11 1984-12-04 Linder Bjoern H Oxide anode for use in impressed current cathodic corrosion protection
US4710644A (en) * 1985-10-30 1987-12-01 Corrpro Companies, Inc. Replaceable deep anode system
EP0224851A1 (en) * 1985-11-27 1987-06-10 Heraeus Elektroden GmbH Electrode for electrochemical processes
US4966675A (en) * 1988-03-15 1990-10-30 Steininger Karl Heinz Polarizable electrode
US5584975A (en) * 1995-06-15 1996-12-17 Eltech Systems Corporation Tubular electrode with removable conductive core
GB2309978A (en) * 1996-02-09 1997-08-13 Atraverda Ltd Titanium suboxide electrode; cathodic protection

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2511266C1 (en) * 2012-10-30 2014-04-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Челябинская государственная агроинженерная академия" Device for cleaning agricultural soil from pesticides

Also Published As

Publication number Publication date
HK1120294A1 (en) 2009-03-27
GB9917015D0 (en) 1999-09-22
RU2247175C2 (en) 2005-02-27
CN101135057B (en) 2012-02-01
GB9915420D0 (en) 1999-09-01
CN101135057A (en) 2008-03-05
GB2351739B (en) 2004-01-21

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Effective date: 20120720