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US3469074A - Method of electrically heating an aqueous electrolyte - Google Patents

Method of electrically heating an aqueous electrolyte Download PDF

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Publication number
US3469074A
US3469074A US370115A US3469074DA US3469074A US 3469074 A US3469074 A US 3469074A US 370115 A US370115 A US 370115A US 3469074D A US3469074D A US 3469074DA US 3469074 A US3469074 A US 3469074A
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US
United States
Prior art keywords
titanium
electrode
electrodes
iridium
rhodium
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.)
Expired - Lifetime
Application number
US370115A
Inventor
Joseph Bernard Cotton
Brenda Sanderson
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.)
Imperial Metal Industries Kynoch Ltd
Original Assignee
Imperial Metal Industries Kynoch 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
Priority claimed from GB2193663A external-priority patent/GB1068732A/en
Application filed by Imperial Metal Industries Kynoch Ltd filed Critical Imperial Metal Industries Kynoch Ltd
Application granted granted Critical
Publication of US3469074A publication Critical patent/US3469074A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B1/00Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
    • H01B1/02Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors mainly consisting of metals or alloys

Definitions

  • the electrode consists of a coating of iridium, rhodium or alloys thereof, especially alloys with platinum, painted or plated on a titanium base.
  • the electrodes are for use with an alternating current and have the advantage that the electrode will not corrode even if the said coating is pervious and contains pores.
  • a soluble alkali metal phosphate be dissolved in the water.
  • This invention relates to electrode boilers and in particular to electrodes for use in and a method of operation of such boilers.
  • Electrode boilers are usually operated by alternating current and the electrodes must be constructed of a material which is capable of passing a high current to the electrolyte, usually water, without corroding.
  • a material which is capable of passing a high current to the electrolyte usually water, without corroding.
  • the materials which have been proposed for use as electrodes for such boilers are cast iron, silicon-iron, nickel-copper alloys, copper-base alloys, aluminium and stainless steel, but it has been found that corrosion in various degrees occurs dependent upon the characteristics of the water.
  • an electrode in which at least the surfaces for passing a current into an electrolyte consist of iridium or rhodium or of an alloy of iridium and rhodium or of an alloy of iridium or rhodium and platinum or of an alloy of iridium and rhodium and platinum.
  • such an electrode may comprise a construction of titanium or a titanium-base alloy coated at least on such surfaces with one of said metals or alloys hereinafter referred to as iridium, rhodium or their specified alloys.
  • Platinum itself is effective as an electrode surface for only a short time because the metal oxidises and it is clearly uneconomic.
  • Platinum coated by either plating or painting titanium is likewise unsatisfactory, because the platinum quickly strips off. If partially coated titanium anodes are used, the bare titanium corrodes, particularly in the presence of chlorides.
  • An electrode in accordance with the invention may be constructed by making the electrode shape from titanium or titanium-base alloy and coating the surfaces from which the current is to pass to the electrolyte by plating or painting with iridium, rhodium or their specified alloys. Such alloys are commercially prepared as paints.
  • the electrode may be in the form of a wire mesh or a sheet of iridium, rhodium or their specified alloys.
  • the immersed portions of the conductors to the electrodes may be made from titanium or titanium-base alloy provided the method of operating the boiler is modified as hereinafter described to prevent corrosion of the titanium, particularly in the presence of chlorides.
  • the use of titanium conductors which act also as supports for the actual electrodes clearly is advantageous and simplifies construction.
  • water containing chlorides can be heated or boiled at commercial voltages without corrosion of uncoated titanium used in the construction of the electrodes occurring and this is achieved by providing conditions in the boiler in which a protective film is maintained on the titanium. Such conditions prevail when the water contains a soluble phosphate.
  • a suitable soluble phosphate is an alkali metal hexametaphosphate, preferably the sodium compound commercially available under the registered Trademark Calgon. An addition of 0.2% w/v (2 gms./litre) of sodium hexametaphosphate has been found to be satisfactory. Where it is desired to boil deionised water, the same amount of sodium hexametaphosphate may be used to impart sufiicient conductivity to the water without risk of corroding the electrodes.
  • an electrode boiler having A5" diameter commercially pure titanium electrodes completely coated with iridium spaced 6" apart and immersed 3 was used.
  • Three litres of water of the above compositions was boiled efficiently and maintained at boiling point for 300 hours using an AC. 240 volt, 50 cycles/ second supply at a current of 0.8 amp. when cold rising to 2.0 amps. at boiling point. No corrosion of the electrode occurred.
  • a method of heating an aqueous electrolyte comprising at least partially immersing in said electrolyte at &
  • At least two electrodes which have a base support material selected from the group consisting of titanium and titanium-base alloys, and a coating on said base support material selected from the group consisting of iridium, rhodium, and alloys thereof, and iridium, rhodium and alloys thereof further alloyed with platinum, and applying an alternating current to the electrodes, and wherein a soluble phosphate in an amount of at least about 0.2% weight/volume is added to the aqueous electrolyte when chlorides are contained in the electrolyte.
  • soluble phosphate is an alkali metal hexametaphosphate.

Landscapes

  • Prevention Of Electric Corrosion (AREA)
  • Electrolytic Production Of Metals (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

United States Patent O 3,469,074 METHOD OF ELECTRICALLY HEATING AN AQUEOUS ELECTROLYTE Joseph Bernard Cotton and Brenda Sanderson, Sutton Coldfield, England, assignors to Imperial Metal Industries (Kynoch) Limited, London, England, a corporation of Great Britain No Drawing. Filed May 25, 1964, Ser. No. 370,115 Claims priority, application Great Britain, May '31, 1963, 21,936/63 Int. Cl. H05b 3/60 US. Cl. 219-284 3 Claims ABSTRACT OF THE DISCLOSURE There is provided an electrode and process of using the electrode as a heating element in boilers. The electrode consists of a coating of iridium, rhodium or alloys thereof, especially alloys with platinum, painted or plated on a titanium base. The electrodes are for use with an alternating current and have the advantage that the electrode will not corrode even if the said coating is pervious and contains pores. When water containing chlorides is used in such a boiler, it is preferred that a soluble alkali metal phosphate be dissolved in the water.
This invention relates to electrode boilers and in particular to electrodes for use in and a method of operation of such boilers.
Electrode boilers are usually operated by alternating current and the electrodes must be constructed of a material which is capable of passing a high current to the electrolyte, usually water, without corroding. Among the materials which have been proposed for use as electrodes for such boilers are cast iron, silicon-iron, nickel-copper alloys, copper-base alloys, aluminium and stainless steel, but it has been found that corrosion in various degrees occurs dependent upon the characteristics of the water.
According to the invention there is provided an electrode in which at least the surfaces for passing a current into an electrolyte consist of iridium or rhodium or of an alloy of iridium and rhodium or of an alloy of iridium or rhodium and platinum or of an alloy of iridium and rhodium and platinum.
Conveniently, such an electrode may comprise a construction of titanium or a titanium-base alloy coated at least on such surfaces with one of said metals or alloys hereinafter referred to as iridium, rhodium or their specified alloys.
An alloy of 30% iridium and 70% platinum has been found to be satisfactory.
Platinum itself is effective as an electrode surface for only a short time because the metal oxidises and it is clearly uneconomic.
Platinum coated by either plating or painting titanium is likewise unsatisfactory, because the platinum quickly strips off. If partially coated titanium anodes are used, the bare titanium corrodes, particularly in the presence of chlorides.
An electrode in accordance with the invention may be constructed by making the electrode shape from titanium or titanium-base alloy and coating the surfaces from which the current is to pass to the electrolyte by plating or painting with iridium, rhodium or their specified alloys. Such alloys are commercially prepared as paints.
The electrode may be in the form of a wire mesh or a sheet of iridium, rhodium or their specified alloys.
The immersed portions of the conductors to the electrodes may be made from titanium or titanium-base alloy provided the method of operating the boiler is modified as hereinafter described to prevent corrosion of the titanium, particularly in the presence of chlorides. The use of titanium conductors which act also as supports for the actual electrodes clearly is advantageous and simplifies construction.
When an alternating current is being conducted between tWo titanium electrodes immersed in water, the protective film on the surface of the titanium will break down and corrosion will ensue when appreciable quantities of chlorides are present and voltages are greater than 8-10 volts D.C. or between -250 volts A.C. These A.C. voltages are those most frequently met with commercially and would normally be used for electrode boilers at a fairly high current density.
By the modification of the method of operating an electrode boiler referred to above, water containing chlorides can be heated or boiled at commercial voltages without corrosion of uncoated titanium used in the construction of the electrodes occurring and this is achieved by providing conditions in the boiler in which a protective film is maintained on the titanium. Such conditions prevail when the water contains a soluble phosphate.
A suitable soluble phosphate is an alkali metal hexametaphosphate, preferably the sodium compound commercially available under the registered Trademark Calgon. An addition of 0.2% w/v (2 gms./litre) of sodium hexametaphosphate has been found to be satisfactory. Where it is desired to boil deionised water, the same amount of sodium hexametaphosphate may be used to impart sufiicient conductivity to the water without risk of corroding the electrodes.
Tests have been carried out on a water having the following composition:
Parts per million Conductivity 680 recip. megohms.
When such a water is boiled using A0. at 240 volts and a current of 2.0 amps. corrosion of a pair of titanium electrodes occurs.
In an example of the invention an electrode boiler having A5" diameter commercially pure titanium electrodes completely coated with iridium spaced 6" apart and immersed 3 was used. Three litres of water of the above compositions was boiled efficiently and maintained at boiling point for 300 hours using an AC. 240 volt, 50 cycles/ second supply at a curent of 0.8 amp. when cold rising to 2.0 amps. at boiling point. No corrosion of the electrode occurred.
A similar procedure was carried out using electrodes completely coated with 70% platinum, 30% iridium and electrodes completely coated with rhodium without corrosion occurring. The rhodium-coated electrodes were tested for more than 2000 hours.
Other conventional electrode materials, as before mentioned, corrode under such conditions even in the presence of the soluble phosphate.
We claim:
1. A method of heating an aqueous electrolyte comprising at least partially immersing in said electrolyte at &
least two electrodes which have a base support material selected from the group consisting of titanium and titanium-base alloys, and a coating on said base support material selected from the group consisting of iridium, rhodium, and alloys thereof, and iridium, rhodium and alloys thereof further alloyed with platinum, and applying an alternating current to the electrodes, and wherein a soluble phosphate in an amount of at least about 0.2% weight/volume is added to the aqueous electrolyte when chlorides are contained in the electrolyte.
2. A method as claimed in claim 1 in which the soluble phosphate is an alkali metal hexametaphosphate.
3. A method as claimed in claim 2 in which sodium hexametaphosphate is present in an amount equivalent to 0.2% weight in volume.
4 References Cited UNITED STATES PATENTS 12/1926 Dantsizen 219-284 2/1954 Livingstone 219-284 5/1964 Miller et al. 204-496 4/1967 Teel 204-280 X FOREIGN PATENTS 1/ 1946 Great Britain. 4/ 1953 Great Britain.
ANTHONY BARTIS, Primary Examiner US. Cl. X.R.
US370115A 1963-05-31 1964-05-25 Method of electrically heating an aqueous electrolyte Expired - Lifetime US3469074A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB2193663A GB1068732A (en) 1963-05-31 1963-05-31 Electrode boiler
BE648655A BE648655A (en) 1963-05-31 1964-05-29

Publications (1)

Publication Number Publication Date
US3469074A true US3469074A (en) 1969-09-23

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ID=25655929

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Application Number Title Priority Date Filing Date
US370115A Expired - Lifetime US3469074A (en) 1963-05-31 1964-05-25 Method of electrically heating an aqueous electrolyte

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US (1) US3469074A (en)
BE (1) BE648655A (en)
DE (1) DE1279868B (en)
NL (1) NL6406118A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3666917A (en) * 1969-12-12 1972-05-30 Hydroflow Corp Heating system utilizing an electrolytic device in a closed hydraulic circuit
US3775284A (en) * 1970-03-23 1973-11-27 J Bennett Non-passivating barrier layer electrodes
US4049513A (en) * 1975-03-17 1977-09-20 Erco Industries Limited Treatment of cell anodes
US4422917A (en) * 1980-09-10 1983-12-27 Imi Marston Limited Electrode material, electrode and electrochemical cell

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1610751A (en) * 1924-02-19 1926-12-14 Gen Electric Electric boiler and method of operation
GB574909A (en) * 1943-07-24 1946-01-25 Arthur Norman Jackson Improvements in or relating to, electric heaters for liquids
GB690693A (en) * 1950-01-03 1953-04-29 Gen Electric Co Ltd Improvements in or relating to immersion electrodes for the heating of electrically conducting liquids
US2668225A (en) * 1951-03-20 1954-02-02 Livingstone Engineering Compan Vaporizable liquid electrode boiler
US3133872A (en) * 1959-03-10 1964-05-19 Chemionics Engineering Lab Inc Anode for electrochemical applications
US3313721A (en) * 1958-12-31 1967-04-11 Englehard Ind Inc Dish-shaped anode

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE170175C (en) *
CH101816A (en) * 1922-10-30 1923-12-01 Alfred Dr Schmid Electrode.
US2434731A (en) * 1943-11-16 1948-01-20 Baker & Co Inc Platinum sheet electrode
AT219564B (en) * 1957-04-09 1962-02-12 Curacaosche Exploitatie Mij Ut Anode, especially for alkali chlorine electrolysis, consisting of a core of base metal which is covered with a cover layer of a noble metal
DE1105395B (en) 1959-09-24 1961-04-27 Hoechst Ag Metal anode for the electrolytic separation of chlorine

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1610751A (en) * 1924-02-19 1926-12-14 Gen Electric Electric boiler and method of operation
GB574909A (en) * 1943-07-24 1946-01-25 Arthur Norman Jackson Improvements in or relating to, electric heaters for liquids
GB690693A (en) * 1950-01-03 1953-04-29 Gen Electric Co Ltd Improvements in or relating to immersion electrodes for the heating of electrically conducting liquids
US2668225A (en) * 1951-03-20 1954-02-02 Livingstone Engineering Compan Vaporizable liquid electrode boiler
US3313721A (en) * 1958-12-31 1967-04-11 Englehard Ind Inc Dish-shaped anode
US3133872A (en) * 1959-03-10 1964-05-19 Chemionics Engineering Lab Inc Anode for electrochemical applications

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3666917A (en) * 1969-12-12 1972-05-30 Hydroflow Corp Heating system utilizing an electrolytic device in a closed hydraulic circuit
US3775284A (en) * 1970-03-23 1973-11-27 J Bennett Non-passivating barrier layer electrodes
US4049513A (en) * 1975-03-17 1977-09-20 Erco Industries Limited Treatment of cell anodes
US4422917A (en) * 1980-09-10 1983-12-27 Imi Marston Limited Electrode material, electrode and electrochemical cell

Also Published As

Publication number Publication date
DE1279868B (en) 1968-10-10
BE648655A (en) 1964-11-30
NL6406118A (en) 1964-12-01

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