US3469074A - Method of electrically heating an aqueous electrolyte - Google Patents
Method of electrically heating an aqueous electrolyte Download PDFInfo
- 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
- Authority
- 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
Links
- 238000000034 method Methods 0.000 title description 10
- 239000003792 electrolyte Substances 0.000 title description 9
- 238000010438 heat treatment Methods 0.000 title description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 18
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 16
- 239000010936 titanium Substances 0.000 description 16
- 229910052719 titanium Inorganic materials 0.000 description 16
- 229910045601 alloy Inorganic materials 0.000 description 15
- 239000000956 alloy Substances 0.000 description 15
- 239000010948 rhodium Substances 0.000 description 12
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 229910052741 iridium Inorganic materials 0.000 description 10
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 10
- 229910052697 platinum Inorganic materials 0.000 description 9
- 229910052703 rhodium Inorganic materials 0.000 description 9
- 239000002585 base Substances 0.000 description 8
- 238000005260 corrosion Methods 0.000 description 7
- 230000007797 corrosion Effects 0.000 description 7
- 150000001805 chlorine compounds Chemical class 0.000 description 6
- 229910019142 PO4 Inorganic materials 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 5
- 239000010452 phosphate Substances 0.000 description 5
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 4
- 229910000575 Ir alloy Inorganic materials 0.000 description 3
- 229910000629 Rh alloy Inorganic materials 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 3
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 3
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 150000001340 alkali metals Chemical class 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 229940005740 hexametaphosphate Drugs 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000010422 painting Methods 0.000 description 2
- 238000007747 plating Methods 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- 241001490312 Lithops pseudotruncatella Species 0.000 description 1
- 229910000318 alkali metal phosphate Inorganic materials 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- YOCUPQPZWBBYIX-UHFFFAOYSA-N copper nickel Chemical compound [Ni].[Cu] YOCUPQPZWBBYIX-UHFFFAOYSA-N 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- XWHPIFXRKKHEKR-UHFFFAOYSA-N iron silicon Chemical compound [Si].[Fe] XWHPIFXRKKHEKR-UHFFFAOYSA-N 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 150000003388 sodium compounds Chemical class 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/02—Conductors 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.
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 |
Family
ID=25655929
Family Applications (1)
| 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 |
Country Status (4)
| Country | Link |
|---|---|
| US (1) | US3469074A (en) |
| BE (1) | BE648655A (en) |
| DE (1) | DE1279868B (en) |
| NL (1) | NL6406118A (en) |
Cited By (4)
| 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)
| 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)
| 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 |
-
1964
- 1964-05-25 US US370115A patent/US3469074A/en not_active Expired - Lifetime
- 1964-05-29 DE DEJ25936A patent/DE1279868B/en not_active Withdrawn
- 1964-05-29 NL NL6406118A patent/NL6406118A/xx unknown
- 1964-05-29 BE BE648655A patent/BE648655A/xx unknown
Patent Citations (6)
| 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)
| 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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