US2495466A - Packaged magnesium anode with cemented backfill - Google Patents
Packaged magnesium anode with cemented backfill Download PDFInfo
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- US2495466A US2495466A US765048A US76504847A US2495466A US 2495466 A US2495466 A US 2495466A US 765048 A US765048 A US 765048A US 76504847 A US76504847 A US 76504847A US 2495466 A US2495466 A US 2495466A
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- anode
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- backfill
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- 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
- 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
-
- 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
- C23F2201/00—Type of materials to be protected by cathodic protection
- C23F2201/02—Concrete, e.g. reinforced
-
- 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
- C23F2213/20—Constructional parts or assemblies of the anodic or cathodic protection apparatus
- C23F2213/22—Constructional parts or assemblies of the anodic or cathodic protection apparatus characterized by the ionic conductor, e.g. humectant, hydratant or backfill
Definitions
- This invention relates to improved packaged anodes forthe. galvanic protection. of underground metals. 'It also concerns protection systems using such-anodes.
- Fig. 1 is a schematic vertical section showing the manner "(if using one form of the new packaged anode in the galvanic protectionof a buried pipeline;
- Fig. 2 is a vertical section through another form of packaged anode along the line. 2-2 in Fig. 3;
- Fig. 3 is 'a horizontal section through'the article of Fig, 2 along the line 33 in Fig. 2.
- the packaged anodes of theinvention the .magnesium metal anode i'simbedded in a unitary self-sustaining backfill' consisting 'of a cemented mass of a finely-divided or granular non-acidic solid electrolyte.
- the anode metal encased in a body of porous stone-like material which is of such composition and size as to 6 Claims. (01. 204-197) 2 provide a suitable electrolytic environment for the anode.
- any granular or powdered non-acidic solid electrolyte may be used in making the new packaged anodes, since the major func tion of this material is simply to render the backfill electrolytically conductive.
- alkaline earth metal hydroxides and alkalior alkaline-earth metal salts of acids which form watersoluble magnesium salts, or mixtures of these substances are preferred. It is particularly advantageous to select an electrolyte which is only sparingly soluble'in water, i. e. one having a solubility from about 0.1 to about 2 percent by weight at atmospheric temperatures.
- Calcium sulfate usually in the form of gypsum (CaSOaZI-IZO) or calcined gypsum, is perhaps the best choice because of its low cost and excellent performance, although magnesium sulfite is also very satisfactory.
- the material'used to bind together the particles of finely-divided electrolyte in making the new packaged anode may be any non-acidic inorganic cement capable of setting in the presence of water.
- Plaster of Paris calcined gypsum
- hydraulic cements such as Portland cement, and magnesia cements, especially magnesium oxysulfate and oxychloride, are preferred.
- the proportion of cement used is not critical, but should be sufficient to insure that the electrolyte is cemented together to a unitary mass of good strength. In general, the cement should constitute at least 10 percent by weight, and better 20 to 30 percent, of the total dry constituents of the backfill.
- the backfill composition for the new packaged anodes may also contain minor proportions ofother nonacidic materialaefg. sand, gravel, crushed washed coke; and other electrolytically inert fillers.
- Granular magnesium hydroxide or oxide may be added, each having the desirable effect or assisting in maintaining alkalinity.
- Powdered or granular vbentonite-,(montmorillonite, a sodium-type base-exchange. volcanic clay) is also advantageous in that it tends to absorb and retain water and to retard leaching of the electrolyte.
- the electrolyte, cemenuand filler, if any, are separately ground to coarse powder form and are then mixed.
- the mixture is then stirred into water to form a thick slurry, which .is poured around the magnesium anode while the latter is centered in a .mold.
- the mold may be taken off, leaving the packaged anode ready for use. It is desirable, to secure a cemented backfill of good porosity,-to use rather coarsely ground materials.
- FIG. 1 A typical installation for cathodic protection, using a packaged anode according to the invention, is shown in Fig. 1, in which a steel pipeline 4 buried in the earth is being protected.
- the packaged anode 5 is made of an elongated cylindrical body of magnesium 6 cast around a core formed by part of a steel cable I, the other portion of which extends beyond the anode to con-1 stitute an electrical lead-wire.
- the magnesium -& is imbedded in a backfill consisting of a cemented block 8 formed by ground gypsum bound together by magnesium oxysulfate. As shown, the block 8 and its contained anode 6 are buried in the earth near the pipeline 4, with the cable 1 being connected electrically to the pipe by a conductor 9.
- a suitable hole is dug, the packaged anode 5 is lowered in place, and earth is tamped around it.
- the electrical conductor to the pipeline is then installed and buried.
- the start of electrolytic action may be hastened by pouring water around the spot where the anode is buried.
- the backfill may contain reinforcing to strengthen the cemented mass.
- Preferred reinforcing materials are flexible non-conductors, most suitably porous fabrics such as burlap or canvas.
- a typical construction of this sort is shown in Figs. 2 and 3 in which the magnesium anode E is imbedded in a mass In of ground gypsum cemented together by Portland cement which is reinforced by burlap ll wrapped spirally around the anode.
- a suitable length of burlap is laid on a flat surface and a settable mixture of gypsum and Portland cement is spread over it as a thick layer.
- the anode is then laid on top at one end and is rolled along the surface to wrap the burlap and cement mixture around the anode. After the cement has set, the article is ready for use.
- the number and size of anodes and the quantity of backfill required to secure effective cathodic protection of a given pipeline or other structure are determined by well-known engineering principles.
- Ewample 1 Packaged anodes were prepared in the manner illustrated in Figs. 2 and 3, using magnesium rods as anodes and canvas as reinforcing. The
- backfill consisted of a mixture of: ground gyp- 7 Packaged anodes were made up as in Example 1, except that the cementable backfill mixture was: ground gypsum, '70 parts, and magnesium sulfite 5 parts as electrolytes; ground bentonite, 5 parts, as filler; and magnesium oxide, 10 parts,
- magnesium sulfate 5 parts, as cement.
- Example 3 Packaged anodes were made up as in Example 1, except that the backfill mixture was: ground gypsum, 20 parts, and magnesium sulfite, 2 parts as electrolytes; silica sand, 58 parts, as filler; and magnesium oxide, 20 parts, and magnesium sulfate, 8 parts, as cement.
- Example 4 Packaged anodes were made up as in Example 1, except that the backfill was: ground gypsum, 40 parts, and magnesium sulfite, 2 parts, as electrolytes; silica sand, 36 parts, and bentonite, 2 parts, as fillers; and Portland cement, 20 parts, as cement. This mixture was wetted with a 12 B. magnesium sulfate aqueous. solution instead ,of with water when it was being applied to the anodes.
- the sacrificial anodes may be either of magnesium or of a magnesium-base alloy, both being comprehended by the term magnesium meta as used in the claims.
- a packaged anode for use in cathodic protection systems comprising a magnesium metal anode imbedded in a self-sustaining porous mass of a granular electrolyte selected fromthe class consisting of alkaline earth metal hydroxides and alkaliand alkaline-earth metal salts of acids which form water-soluble magnesium salts cemented together by magnesium oxysulfate.
- a packaged anode for use in cathodic protection systems comprising a magnesium metal anode imbedded in a set mass consisting essentially of granular ypsum cemented together by magnesium oxysulfate.
- a cathodic protection system comprising a packaged anode as defined in claim 1 buried in the earth near the structure and electrically connected thereto.
Description
Patented Jan. 24, 1950 PACKAGED MAGNESIUM ANODE WITH CEMENTED BACKFILL Herman H. Miller, Midland, Mich., assignor to The Dow Chemical Company, Midland, Mich., a corporation of Delaware Application July 31, 1947, Serial No. 765,048
I This invention relates to improved packaged anodes forthe. galvanic protection. of underground metals. 'It also concerns protection systems using such-anodes.
. ,In galvanic systems for thecathodic protection of pipelines and. other underground structures, sacrificial electrodes of a metal anodic to the structurasucli as magnesium, are buried in the earth near thestructureand are connected to itfby electrical conductors. The resulting flow of current maintains the structure cathodic with respect to thesoil and greatly minimizes its corrosion. Since magnesium tends to be. consumed uselessly when indirect'contact'with some types of soils, it is customary, in using this Illetalas a sacrificial anode, to 'bury it in -a prepared bed or backfill. designed to control the chemical nature of the anode environment.
In prior. practice, such backfills have consisted of powder mixtures, e. g. of gypsum and bentonite, which have been tamped in place around the .anode when it is being buried. In general, these backfill is associated with a magnesium anode in a unit package which can be installed simply by burying it. Another object is to provide a packa edanode in which loose powder is not present and a special container is not required, the backflll itself having a fixed'formand being of sufficient mechanical strength to withstand'stresse incident to shipment and installation. The invention will be explained with reference to the accompanying drawing, .inwhich Fig. 1 is a schematic vertical section showing the manner "(if using one form of the new packaged anode in the galvanic protectionof a buried pipeline;
.Fig. 2 is a vertical section through another form of packaged anode along the line. 2-2 in Fig. 3; and
Fig. 3 is 'a horizontal section through'the article of Fig, 2 along the line 33 in Fig. 2.
In the packaged anodes of theinvention, the .magnesium metal anode i'simbedded in a unitary self-sustaining backfill' consisting 'of a cemented mass of a finely-divided or granular non-acidic solid electrolyte. In efiect, then, the anode metal encased in a body of porous stone-like material which is of such composition and size as to 6 Claims. (01. 204-197) 2 provide a suitable electrolytic environment for the anode.
In so far as known, any granular or powdered non-acidic solid electrolyte may be used in making the new packaged anodes, since the major func tion of this material is simply to render the backfill electrolytically conductive. In general, alkaline earth metal hydroxides and alkalior alkaline-earth metal salts of acids which form watersoluble magnesium salts, or mixtures of these substances, are preferred. It is particularly advantageous to select an electrolyte which is only sparingly soluble'in water, i. e. one having a solubility from about 0.1 to about 2 percent by weight at atmospheric temperatures. Calcium sulfate, usually in the form of gypsum (CaSOaZI-IZO) or calcined gypsum, is perhaps the best choice because of its low cost and excellent performance, although magnesium sulfite is also very satisfactory.
The material'used to bind together the particles of finely-divided electrolyte in making the new packaged anode may be any non-acidic inorganic cement capable of setting in the presence of water. Plaster of Paris (calcined gypsum), hydraulic cements; such as Portland cement, and magnesia cements, especially magnesium oxysulfate and oxychloride, are preferred. The proportion of cement used is not critical, but should be sufficient to insure that the electrolyte is cemented together to a unitary mass of good strength. In general, the cement should constitute at least 10 percent by weight, and better 20 to 30 percent, of the total dry constituents of the backfill.
In addition to electrolyte and cement, the backfill composition for the new packaged anodes may also contain minor proportions ofother nonacidic materialaefg. sand, gravel, crushed washed coke; and other electrolytically inert fillers. Granular magnesium hydroxide or oxide may be added, each having the desirable effect or assisting in maintaining alkalinity. Powdered or granular vbentonite-,(montmorillonite, a sodium-type base-exchange. volcanic clay) is also advantageous in that it tends to absorb and retain water and to retard leaching of the electrolyte.
In a preferred method of making packaged anodes according to the invention, the electrolyte, cemenuand filler, if any, are separately ground to coarse powder form and are then mixed. The mixture is then stirred into water to form a thick slurry, which .is poured around the magnesium anode while the latter is centered in a .mold. After the slurry has set, the mold may be taken off, leaving the packaged anode ready for use. It is desirable, to secure a cemented backfill of good porosity,-to use rather coarsely ground materials.
While, in the foregoing, the electrolyte and the cement have been discussed separately, it is entirely possible for a. single substance to function as both. For example, it is regarded as within the invention to imbed a magnesium anode in a set mass of plaster of Paris or of magnesium oxysulfate, in which case no other electrolyte or filler need be added.
A typical installation for cathodic protection, using a packaged anode according to the invention, is shown in Fig. 1, in which a steel pipeline 4 buried in the earth is being protected. The packaged anode 5 is made of an elongated cylindrical body of magnesium 6 cast around a core formed by part of a steel cable I, the other portion of which extends beyond the anode to con-1 stitute an electrical lead-wire. The magnesium -& is imbedded in a backfill consisting of a cemented block 8 formed by ground gypsum bound together by magnesium oxysulfate. As shown, the block 8 and its contained anode 6 are buried in the earth near the pipeline 4, with the cable 1 being connected electrically to the pipe by a conductor 9.
In making the installation, a suitable hole is dug, the packaged anode 5 is lowered in place, and earth is tamped around it. The electrical conductor to the pipeline is then installed and buried. In dry soils, the start of electrolytic action may be hastened by pouring water around the spot where the anode is buried.
In an alternative way of making the new packaged anodes, the backfill may contain reinforcing to strengthen the cemented mass. Preferred reinforcing materials are flexible non-conductors, most suitably porous fabrics such as burlap or canvas. A typical construction of this sort is shown in Figs. 2 and 3 in which the magnesium anode E is imbedded in a mass In of ground gypsum cemented together by Portland cement which is reinforced by burlap ll wrapped spirally around the anode.
In making the packaged anode of Figs. 2 and 3, a suitable length of burlap is laid on a flat surface and a settable mixture of gypsum and Portland cement is spread over it as a thick layer. The anode is then laid on top at one end and is rolled along the surface to wrap the burlap and cement mixture around the anode. After the cement has set, the article is ready for use.
In field use of the invention, the number and size of anodes and the quantity of backfill required to secure effective cathodic protection of a given pipeline or other structure are determined by well-known engineering principles.
The following examples will further illustrate the invention.
Ewample 1 Packaged anodes were prepared in the manner illustrated in Figs. 2 and 3, using magnesium rods as anodes and canvas as reinforcing. The
backfill consisted of a mixture of: ground gyp- 7 Packaged anodes were made up as in Example 1, except that the cementable backfill mixture was: ground gypsum, '70 parts, and magnesium sulfite 5 parts as electrolytes; ground bentonite, 5 parts, as filler; and magnesium oxide, 10 parts,
and magnesium sulfate, 5 parts, as cement.
I Example 3 Packaged anodes were made up as in Example 1, except that the backfill mixture was: ground gypsum, 20 parts, and magnesium sulfite, 2 parts as electrolytes; silica sand, 58 parts, as filler; and magnesium oxide, 20 parts, and magnesium sulfate, 8 parts, as cement.
Example 4 Packaged anodes were made up as in Example 1, except that the backfill was: ground gypsum, 40 parts, and magnesium sulfite, 2 parts, as electrolytes; silica sand, 36 parts, and bentonite, 2 parts, as fillers; and Portland cement, 20 parts, as cement. This mixture was wetted with a 12 B. magnesium sulfate aqueous. solution instead ,of with water when it was being applied to the anodes.
All of these anodes were tested in the cathodic protection of iron in natural water and developed adequate currents at good electrochemical efiiciencies.
While the invention has been described as useful in the cathodic protection of underground ferrous metal structures, it is applicable in protecting structures of any corrodible metal cathodic to magnesium. The sacrificial anodes may be either of magnesium or of a magnesium-base alloy, both being comprehended by the term magnesium meta as used in the claims.
What is claimed is:
1. A packaged anode for use in cathodic protection systems comprising a magnesium metal anode imbedded in a self-sustaining porous mass of a granular electrolyte selected fromthe class consisting of alkaline earth metal hydroxides and alkaliand alkaline-earth metal salts of acids which form water-soluble magnesium salts cemented together by magnesium oxysulfate.
2. A packaged anode according to claim 1 wherein the electrolyte has a solubility in Water of from 0.1 to 2 percent by weight at atmospheric temperatures.
3. A packaged anode according to claim 1 wherein the electrolyte is' calcium sulfate.
4. A packaged anode for use in cathodic protection systems comprising a magnesium metal anode imbedded in a set mass consisting essentially of granular ypsum cemented together by magnesium oxysulfate.
5; A packaged anode according to claim 4 wherein the set mass also contains a small proportion of bentonite.
6. In combination with an underground structure of a corrodible metal cathodic'to magnesium, a cathodic protection system comprising a packaged anode as defined in claim 1 buried in the earth near the structure and electrically connected thereto.
HERMAN MILLER.
REFERENCES CITED The following references are of record the file of this patent:
UNITED STATES PATENTS Y Date Number Name 489,668 Bryan Jan. 10, 1893 2,088,307 Ruhofi et al July 27, 1937 OTHER REFERENCES quist, April 1944, page 83.
Claims (1)
1. A PACKAGED ANODE FOR USE IN CATHODIC PROTECTION SYSTEMS COMPRISING A MAGNESIUM METAL ANODE IMBEDDED IN A SELF-SUSTAINING POROUS MASS OF A GRANULAR ELECTROLYTE SELECTED FROM THE CLASS CONSISTING OF ALKALINE EARTH METAL HYDROXIDES AND ALKALI- AND ALKALINE-EARTH METAL SALTS OF ACIDS WHICH FORM WATER-SOLUBLE MAGNESIUM SALTS CEMENTED TOGETHER BY MAGNESIUM OXYSULFATE.
Priority Applications (1)
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US765048A US2495466A (en) | 1947-07-31 | 1947-07-31 | Packaged magnesium anode with cemented backfill |
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US765048A US2495466A (en) | 1947-07-31 | 1947-07-31 | Packaged magnesium anode with cemented backfill |
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Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2621154A (en) * | 1946-10-25 | 1952-12-09 | Aluminum Co Of America | Packaged electrodes for the cathodic protection of metallic underground structures |
US3186931A (en) * | 1962-06-26 | 1965-06-01 | Pure Oil Co | Ferrous electrode |
US3288648A (en) * | 1963-02-04 | 1966-11-29 | Pan American Petroleum Corp | Process for producing electrical energy from geological liquid hydrocarbon formation |
US4511444A (en) * | 1983-09-01 | 1985-04-16 | Columbia Gas Systems Service Corp. | Backfill for magnesium anodes |
US4786388A (en) * | 1987-09-14 | 1988-11-22 | Cathodic Engineering Equipment Company | Ground electrode backfill composition, anode bed and apparatus |
US5433829A (en) * | 1987-10-13 | 1995-07-18 | Pool; Wieberen | Process for the electroreclamation of soil material |
US5505826A (en) * | 1994-11-30 | 1996-04-09 | Haglin; Patrick G. | Hydrophilic anode corrosion control system |
US20040099982A1 (en) * | 2002-08-19 | 2004-05-27 | Sirola D. Brien | Conductive concrete compositions and methods of manufacturing same |
US20060005967A1 (en) * | 2002-08-19 | 2006-01-12 | Sirola D B | Deep well anodes for electrical grounding |
US20070187854A1 (en) * | 2002-08-19 | 2007-08-16 | Sirola D B | Deep well anodes for electrical grounding |
US20130118897A1 (en) * | 2005-10-04 | 2013-05-16 | Gareth Glass | Sacrificial anode and backfill combination |
US11121482B2 (en) | 2017-10-04 | 2021-09-14 | Shore Acres Enterprises Inc. | Electrically-conductive corrosion-protective covering |
US11349228B2 (en) | 2017-08-14 | 2022-05-31 | Shore Acres Enterprises Inc. | Corrosion-protective jacket for electrode |
US11421392B2 (en) | 2019-12-18 | 2022-08-23 | Shore Acres Enterprises Inc. | Metallic structure with water impermeable and electrically conductive cementitous surround |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US489668A (en) * | 1893-01-10 | Electric battery | ||
US2088307A (en) * | 1934-12-08 | 1937-07-27 | Marathon Battery Company | Dry cell, core therefor, and method of producing same |
-
1947
- 1947-07-31 US US765048A patent/US2495466A/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US489668A (en) * | 1893-01-10 | Electric battery | ||
US2088307A (en) * | 1934-12-08 | 1937-07-27 | Marathon Battery Company | Dry cell, core therefor, and method of producing same |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2621154A (en) * | 1946-10-25 | 1952-12-09 | Aluminum Co Of America | Packaged electrodes for the cathodic protection of metallic underground structures |
US3186931A (en) * | 1962-06-26 | 1965-06-01 | Pure Oil Co | Ferrous electrode |
US3288648A (en) * | 1963-02-04 | 1966-11-29 | Pan American Petroleum Corp | Process for producing electrical energy from geological liquid hydrocarbon formation |
US4511444A (en) * | 1983-09-01 | 1985-04-16 | Columbia Gas Systems Service Corp. | Backfill for magnesium anodes |
US4786388A (en) * | 1987-09-14 | 1988-11-22 | Cathodic Engineering Equipment Company | Ground electrode backfill composition, anode bed and apparatus |
US5433829A (en) * | 1987-10-13 | 1995-07-18 | Pool; Wieberen | Process for the electroreclamation of soil material |
US5589056A (en) * | 1987-10-13 | 1996-12-31 | Pool; Wieberen | Process for electroeclamation of soil material |
US5505826A (en) * | 1994-11-30 | 1996-04-09 | Haglin; Patrick G. | Hydrophilic anode corrosion control system |
US20040099982A1 (en) * | 2002-08-19 | 2004-05-27 | Sirola D. Brien | Conductive concrete compositions and methods of manufacturing same |
US20050194576A1 (en) * | 2002-08-19 | 2005-09-08 | Sirola D. B. | Conductive concrete compositions and methods of manufacturing same |
US20060005967A1 (en) * | 2002-08-19 | 2006-01-12 | Sirola D B | Deep well anodes for electrical grounding |
US20070187854A1 (en) * | 2002-08-19 | 2007-08-16 | Sirola D B | Deep well anodes for electrical grounding |
US7578910B2 (en) | 2002-08-19 | 2009-08-25 | Sae Inc. | Deep well anodes for electrical grounding |
US20130118897A1 (en) * | 2005-10-04 | 2013-05-16 | Gareth Glass | Sacrificial anode and backfill combination |
US11349228B2 (en) | 2017-08-14 | 2022-05-31 | Shore Acres Enterprises Inc. | Corrosion-protective jacket for electrode |
US11757211B2 (en) | 2017-08-14 | 2023-09-12 | Shore Acres Enterprises Inc. | Electrical grounding assembly |
US11121482B2 (en) | 2017-10-04 | 2021-09-14 | Shore Acres Enterprises Inc. | Electrically-conductive corrosion-protective covering |
US11894647B2 (en) | 2017-10-04 | 2024-02-06 | Shore Acres Enterprises Inc. | Electrically-conductive corrosion-protective covering |
US11421392B2 (en) | 2019-12-18 | 2022-08-23 | Shore Acres Enterprises Inc. | Metallic structure with water impermeable and electrically conductive cementitous surround |
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