Patent Grant
11193211
The present invention relates generally to the protection of metallic structures or surfaces prone to corrosion and, in particular, this invention relates to cathodic protection for wood veneer dryers and methods for reducing corrosion of wood veneer dyers.
Single and multiple deck conveyor dryers for reducing the moisture content of sheet materials, including green (or wet) wood veneer, wherein the material being dried is conveyed through a stationary drying chamber while heated gases are circulated through the drying chamber, are well-known in the art. Evaporation of moisture, inorganic compounds, and/or organic compounds (i.e. volatile organic compounds (V.O.C.'s)) from the material being dried causes a build-up of steam within the dryer, which may condense with carbon dioxide to form a corrosive liquid on the walls of the veneer dryer and on other equipment. Many metals corrode due to exposure to moisture and corrosion of metallic structures and surfaces of the dryer has been a major problem in the veneer drying art.
It is desirable to control the corrosion of metallic structures and surfaces of a wood veneer dryer to extend the lifetime of the dryer. To reduce corrosion, metallic structures and surfaces inside of veneer dryers may be made from or coated with corrosion-resistant alloys, such as stainless steel. However, corrosion-resistant alloys are typically expensive. Furthermore, moisture is not precluded from migrating into dryer panel cracks or missed welds not treated with the corrosion-resistant alloy. There is accordingly a need in the art for a wood veneer dryer wherein the metallic structures and surfaces inside the dryer susceptible to corrosion are protected.
Cathodic protection is known in the art to control the corrosion of a metal by making it the cathode of an electrolytic cell. The metal to be protected is connected to a more easily corroded “sacrificial” metal that acts as the anode. The sacrificial metal then corrodes instead of the protected metal. The driving force for the cathodic protection current is the difference in electrode potential between the anode and the cathode.
A cathodic protection system is essentially a closed electric circuit that requires an anode and cathode to be immersed in an electrolyte; hence, cathodic protection is not used to prevent atmospheric corrosion. Typically, the structure to be protected is immersed in a body of fresh or salt water or is buried in moisture-rich soil.
In practice, the main use of cathodic protection is to protect steel structures immersed in a body of water or buried in moisture-rich soil (for example, the exterior surfaces of pipelines, ships' hulls, jetties, foundation piling, steel sheet piling, offshore platforms, and the interior surfaces of water-storage tanks and water-circulating systems).
Due to high maintenance and installation costs, cathodic protection is typically considered to be prohibitively expensive for use with relatively small scale structures, such as wood veneer dryers. Use is further limited by the need for structures to be immersed in a body of water or buried in moisture-rich soil.
The foregoing examples of the related art and limitations related thereto are intended to be illustrative and not exclusive. Other limitations of the related art will become apparent to those of skill in the art upon a reading of the specification and a study of the drawings.
The following embodiments and aspects thereof are described and illustrated in conjunction with systems, tools, and methods which are meant to be exemplary and illustrative, not limiting in scope. In various embodiments, one or more of the above-described problems have been reduced or eliminated, while other embodiments are directed to other improvements.
One aspect of the present invention provides a cathodic protection system for use with a wood veneer dryer. The cathodic protection system includes a DC power supply and an anode mounted inside the veneer dryer in a position to be electrolytically coupled to metallic structures or surfaces inside the veneer dryer when an electrolytic medium is present. The DC power supply has a positive pole electrically connected to the anode and a negative pole electrically connected to the metallic structures or surfaces inside the veneer dryer.
In some embodiments, the anode is more electronegative than the metallic structures or surfaces.
In some embodiments, the anode comprises one or more of high silicon iron, graphite, mixed metal, oxides, lead alloys, platinum, zinc, aluminum, magnesium, cadmium, niobium, tantalum, titanium, ruthenium, ruthenium oxide, rhodium, and rhodium oxide, preferably niobium.
In some embodiments, the anode comprises a niobium ribbon.
In some other embodiments, the anode is coated with a material that is more electronegative than the metallic structures and surfaces.
In some embodiments, the material comprises one or more of high silicon iron, graphite, mixed metal oxides, lead alloys, platinum, zinc, aluminum, magnesium, cadmium, niobium, tantalum, titanium, ruthenium, ruthenium oxide, rhodium, and rhodium oxide, preferably niobium.
In some embodiments, the anode comprises a niobium-coated ribbon.
In some embodiments, the anode is wrapped in an air-permeable membrane.
In some embodiments, the air-permeable membrane comprises one or more of a mineral wool, glass fibers, ceramics, and clays, preferably mineral wool.
In some embodiments, the anode extends from an input end to an output end of the veneer dryer inside a drying chamber.
In some embodiments, the cathodic protection system further includes a computer system to monitor the conditions inside the veneer dryer and to adjust the amount of current supplied by the DC power supply based on the detected conditions.
In some embodiments, the DC power supply supplies an amount of current to the anode and metallic structures or surfaces inside the veneer dryer to shift the potential of the metallic structures or surfaces within the range of about (−) 0.700 V vs. silver/silver chloride (Ag/AgCl) to about (−) 1.200 V vs. silver/silver chloride (Ag/AgCl), preferably about (−) 0.800 V vs. silver/silver chloride (Ag/AgCl) or about (−) 0.950 V vs. silver/silver chloride (Ag/AgCl).
In some other embodiments, the DC power supply supplies an amount of current to the anode and metallic structures or surfaces inside the veneer dryer based on one or more of pH, temperature, electrolytic medium concentration, and electrolytic medium conductivity.
In some embodiments, the electrolytic medium comprises a high-humidity atmosphere inside the veneer dryer.
In some embodiments, the anode is mounted in a protective housing inside the veneer dryer.
Another aspect of the present invention provides a method for reducing the corrosion of metallic structures or surfaces inside a wood veneer dryer. The method includes mounting an anode inside a veneer dryer in a position to be electrolytically coupled to the metallic structures or surfaces inside the veneer dryer when an electrolytic medium is present inside the veneer dryer. A positive pole of a DC power supply is electrically connected to the anode and a negative pole of the DC power supply is electrically connected to the metallic structures and surfaces. Green wood veneer is conveyed through the veneer dryer and heated to a temperature sufficient to produce a high-humidity atmosphere inside the veneer dryer. A controlled amount of current is supplied by the DC power supply to electrolytically couple the anode to the metallic structures or surfaces.
In some embodiments, the conditions inside the veneer dryer are monitored and the amount of current supplied by the DC power supply is adjusted based on the detected conditions.
In some embodiments, the amount of current supplied shifts the potential of the metallic structures or surfaces within the range of about (−) 0.700 V vs. silver/silver chloride (Ag/AgCl) to about (−) 1.200 V vs. silver/silver chloride (Ag/AgCl), preferably about (−) 0.800 V vs. silver/silver chloride (Ag/AgCl) or about (−) 0.950 V vs. silver/silver chloride (Ag/AgCl).
In some other embodiments, the amount of current supplied is ascertainable based on one or more of pH, temperature, electrolytic medium concentration, and electrolytic medium conductivity.
In some embodiments, the anode is wrapped in an air-permeable membrane.
In some embodiments, the air-permeable membrane comprises one or more of a mineral wool, glass fibers, ceramics, and clays, preferably mineral wool.
In some embodiments, the anode is more electronegative than the metallic structures or surfaces.
In some embodiments, the anode comprises one or more of high silicon iron, graphite, mixed metal oxides, lead alloys, platinum, zinc, aluminum, magnesium, cadmium niobium, tantalum, titanium, ruthenium, ruthenium oxide, rhodium, and rhodium oxide, preferably niobium.
In some embodiments, the anode comprises a niobium ribbon.
In some other embodiments, the anode is coated with a material that is more electronegative than the metallic structures and surfaces.
In some embodiments, the material comprises one or more of high silicon iron, graphite, mixed metal oxides, lead alloys, platinum, zinc, aluminum, magnesium, cadmium, niobium, tantalum, titanium, ruthenium, ruthenium oxide, rhodium, and rhodium oxide, preferably niobium.
In some embodiments, the anode comprises a niobium-coated ribbon.
In some embodiments, the anode extends from an input end of the veneer dryer to an output end of a drying chamber of the veneer dryer.
In some embodiments, the anode is mounted in a protective housing inside the veneer dryer.
In addition to the exemplary aspects and embodiments described above, further aspects and embodiments will become apparent by reference to the drawings and by study of the following detailed descriptions.
Exemplary embodiments are illustrated in referenced figures of the drawings. It is intended that the embodiments and figures disclosed are to be considered illustrative of the invention rather than restrictive.
Throughout the following description specific details are set forth in order to provide a more thorough understanding to persons skilled in the art. However, well known elements may not have been shown or described in detail to avoid unnecessarily obscuring the disclosure. Accordingly, the description and drawings are to be regarded in an illustrative, rather than a restrictive, sense.
In this specification, the term “cathodic protection” means controlling the corrosion of a metal structure or surface by making it the cathode of an electrolytic cell. The term “electrolytic cell” means a cell consisting of an electrolyte, its container, and two electrodes (i.e. an anode and a cathode), in which a redox reaction between the electrodes and the electrolyte occurs when an electrical current is applied. The term “anode” means an electrode or terminal by which current enters an electrolytic cell. The term “cathode” means an electrode or terminal by which current leaves an electrolytic cell. The term “electrolyte” means a medium capable of conducting current and in which the flow of current is accompanied by the movement of ions. The term “electrolytically coupled” means the coupling of a pair of electrodes in an electrolytic cell through an electrolyte thereby producing a redox reaction when an electrical current is applied to the cell. The term “corrosive medium” means any fluid that is corrosive to, or promotes corrosion of, a metallic structure or surface. The term “electrolytic medium” means any fluid capable of conducting current and in which the flow of current is accompanied by the movement of ions. The term “moisture” means a fluid, including but not limited to steam and/or condensed steam. The term “high-humidity atmosphere” means an atmosphere having a relatively high amount of moisture. The term “input end” in relation to the wood veneer dryer and components thereof means the end wherein wood veneer to be dried is introduced into the dryer, input end seal chamber, drying chamber, intermediary chamber, or cooling chamber. The term “output end” in relation to the wood veneer dryer and components thereof means the end opposite to the input end, i.e. the end wherefrom dried wood veneer exits the dryer, input end seal chamber, drying chamber, intermediary chamber, or cooling chamber. The term “about” means near the stated value (i.e. within +/− 10% of the stated value).
A cathodic protection system 10, as shown in
As the wood veneer to be dried is heated, moisture and inorganic and/or organic compounds (such as V.O.C.'s) are released from the wood veneer producing a high-humidity atmosphere inside veneer dryer 20. The high-humidity atmosphere inside veneer dryer 20 serves as a corrosive medium and/or an electrolytic medium inside veneer dryer 20. The composition of the corrosive medium and/or the electrolytic medium inside veneer dryer 20 will vary depending on the species of wood dried and the conditions found inside veneer dryer 20 (i.e. temperature, pH, humidity, etc.).
Referring to
In some embodiments, anode 30 may be more electronegative than the metallic structures and surfaces inside veneer dryer 20. Based on the conditions found within veneer dryer 20 (for example, temperature and/or pH), anode 30 may comprise one or more of the following materials: high silicon iron, graphite, mixed metal oxides, lead alloys, platinum, zinc, aluminum, magnesium, cadmium, niobium, tantalum, titanium, ruthenium, ruthenium oxide, rhodium, and rhodium oxide, preferably niobium. In some other embodiments, anode 30 may be coated with a material that is more electronegative than the metallic structures and surfaces inside veneer dryer 20. Based on the conditions found within veneer dryer 20 (for example, temperature and/or pH), the coating may comprise one or more of the following materials: high silicon iron, graphite, mixed metal oxides, lead alloys, platinum, zinc, aluminum, magnesium, cadmium, niobium, tantalum, titanium, ruthenium, ruthenium oxide, rhodium, and rhodium oxide, preferably niobium. In some embodiments, anode 30 comprises a niobium-coated wire or a niobium-coated ribbon. In other embodiments, anode 30 comprises niobium or a niobium ribbon. Persons skilled in the art will recognize that anode 30 may be comprised of or coated with any material that exhibits any one or more of the following features: good electrical conduction; a low rate of corrosion; good mechanical properties; the ability to withstand the stresses which they may be subjected to during installation and in service; the ability to be readily fabricated into a variety of shapes; low cost; and/or the ability to withstand high current densities at its surface without forming resistive barrier oxide layers. Niobium, for example, can resist becoming passive (i.e. developing an oxidation layer) at high temperatures and within the voltage range required to operate catalytic protection system 10, while being capable of delivering constant watt density when a current is applied thereto in a closed circuit.
In some embodiments, as shown in
In some embodiments, as shown in
In operation, DC power supply 40 supplies a controlled amount of current to electrolytically couple anode 30 and the metallic structures and/or surfaces inside veneer dryer 20 when an electrolytic medium is present inside veneer dryer 20. The metallic structures and/or surfaces are thereby rendered the cathode of cathodic protection system 10 and protected from corrosion. For example, DC power supply 40 may use low voltage DC current to shift the potential of the metallic structures and/or surfaces inside veneer dryer 20 within the range of about (−) 0.700 V vs. silver/silver chloride (Ag/AgCl) to about (−) 1.200 V vs. silver/silver chloride (Ag/AgCl), preferably about (−) 0.800 V vs. silver/silver chloride (Ag/AgCl) or about (−) 0.950 V vs. silver/silver chloride (Ag/AgCl). Persons skilled in the art will recognize that the amount of current supplied by DC power supply 40 is readily ascertainable based on pH, temperature, the concentration of the electrolytic medium inside veneer dryer 20, and/or the conductivity of the electrolytic medium inside veneer dryer 20.
A computer system (not shown) may be used to monitor the conditions (such as temperature, pH, the concentration of the electrolytic medium, and/or the conductivity of the electrolytic medium) inside veneer dryer 20 and the current supplied by DC power supply 40 may be adjusted based on the detected conditions. The computer system thereby maintains an optimum current output over the life of anode 30. In the event that cathodic protection system 10 fails to operate, the computer system may be used to notify a user.
Interpretation of Terms
Unless the context clearly requires otherwise, throughout the description and the claims:
Words that indicate directions such as “vertical”, “transverse”, “horizontal”, “upward”, “downward”, “forward”, “backward”, “inward”, “outward”, “left”, “right”, “front”, “back”, “top”, “bottom”, “below”, “above”, “under”, and the like, used in this description and any accompanying claims (where present), depend on the specific orientation of the apparatus described and illustrated. The subject matter described herein may assume various alternative orientations. Accordingly, these directional terms are not strictly defined and should not be interpreted narrowly.
Where a component (e.g. a substrate, assembly, device, manifold, etc.) is referred to above, unless otherwise indicated, reference to that component (including a reference to a “means”) should be interpreted as including as equivalents of that component any component which performs the function of the described component (i.e., that is functionally equivalent), including components which are not structurally equivalent to the disclosed structure which performs the function in the illustrated exemplary embodiments described herein.
Specific examples of systems, methods, and apparatus have been described herein for purposes of illustration. These are only examples. The technology provided herein can be applied to systems other than the example systems described above. Many alterations, modifications, additions, omissions, and permutations are possible within the practice of this invention. This invention includes variations on described embodiments that would be apparent to the skilled addressee, including variations obtained by: replacing features, elements and/or acts with equivalent features, elements and/or acts; mixing and matching of features, elements and/or acts from different embodiments; combining features, elements and/or acts from embodiments as described herein with features, elements and/or acts of other technology; and/or omitting combining features, elements and/or acts from described embodiments.
It is therefore intended that the following appended claims and claims hereafter introduced are interpreted to include all such modifications, permutations, additions, omissions, and sub-combinations as may reasonably be inferred. The scope of the claims should not be limited by the preferred embodiments set forth in the examples, but should be given the broadest interpretation consistent with the description as a whole.
This application is a continuation application of co-pending U.S. patent application Ser. No. 14/736,099, filed on Jun. 10, 2015. This patent application is herein incorporated by reference in its entirety, including without limitation, the specification, claims, and abstract, as well as any figures, tables, or drawings thereof.
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| Entry |
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| Number | Date | Country | |
|---|---|---|---|
| 20190211459 A1 | Jul 2019 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 14736099 | Jun 2015 | US |
| Child | 16352034 | US |
