Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B08—CLEANING
  • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
  • B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto 
  • B08B9/02—Cleaning pipes or tubes or systems of pipes or tubes
  • B08B9/027—Cleaning the internal surfaces; Removal of blockages
  • B08B9/04—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes
  • B08B9/053—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction
  • B08B9/055—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction the cleaning devices conforming to, or being conformable to, substantially the same cross-section of the pipes, e.g. pigs or moles
  • B08B9/0553—Cylindrically shaped pigs
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05C—APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05C7/00—Apparatus specially designed for applying liquid or other fluent material to the inside of hollow work
  • B05C7/06—Apparatus specially designed for applying liquid or other fluent material to the inside of hollow work by devices moving in contact with the work
  • B05C7/08—Apparatus specially designed for applying liquid or other fluent material to the inside of hollow work by devices moving in contact with the work for applying liquids or other fluent materials to the inside of tubes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B08—CLEANING
  • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
  • B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto 
  • B08B9/02—Cleaning pipes or tubes or systems of pipes or tubes
  • B08B9/027—Cleaning the internal surfaces; Removal of blockages
  • B08B9/04—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes
  • B08B9/053—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction
  • B08B9/055—Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction the cleaning devices conforming to, or being conformable to, substantially the same cross-section of the pipes, e.g. pigs or moles
• • 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
  • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
  • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
  • C23C18/02—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
  • C23C18/04—Pretreatment of the material to be coated
• • 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
  • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
  • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
  • C23C18/02—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
  • C23C18/12—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material
  • C23C18/1204—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of inorganic material other than metallic material inorganic material, e.g. non-oxide and non-metallic such as sulfides, nitrides based compounds
  • C23C18/1208—Oxides, e.g. ceramics
  • C23C18/1216—Metal oxides
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
  • B05B12/00—Arrangements for controlling delivery; Arrangements for controlling the spray area
  • B05B12/14—Arrangements for controlling delivery; Arrangements for controlling the spray area for supplying a selected one of a plurality of liquids or other fluent materials or several in selected proportions to a spray apparatus, e.g. to a single spray outlet
  • B05B12/1481—Arrangements for controlling delivery; Arrangements for controlling the spray area for supplying a selected one of a plurality of liquids or other fluent materials or several in selected proportions to a spray apparatus, e.g. to a single spray outlet comprising pigs, i.e. movable elements sealingly received in supply pipes, for separating different fluids, e.g. liquid coating materials from solvent or air
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05D3/00—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials
  • B05D3/10—Pretreatment of surfaces to which liquids or other fluent materials are to be applied; After-treatment of applied coatings, e.g. intermediate treating of an applied coating preparatory to subsequent applications of liquids or other fluent materials by other chemical means
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
  • B05D7/22—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to internal surfaces, e.g. of tubes
  • B05D7/222—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to internal surfaces, e.g. of tubes of pipes
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
  • F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
  • F16L2101/00—Uses or applications of pigs or moles
  • F16L2101/10—Treating the inside of pipes
  • F16L2101/12—Cleaning
• • Y—GENERAL 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
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
  • Y02T50/00—Aeronautics or air transport
  • Y02T50/60—Efficient propulsion technologies, e.g. for aircraft

Definitions

• This invention relates to processes and apparatus used for applying coatings to the internal passageways of a fluid process system, particularly tubes and pipes.
• Metal tubes are often used in a variety of industrial processes. Oftentimes there is a need to reduce damage to the inner surfaces of metal tubes in heat exchangers, process systems and similar equipment due to corrosion, erosion, debris accumulation, or a combination thereof. To this end, a protective coating is often the preferred solution.
• a protective coating is often the preferred solution.
• devices for coating the interior of a pipe Methods included in the prior art include brushing, swabbing, spraying, and others. Devices and methods for brushing on an interior coating on a pipe are disclosed in U.S. Pat. Nos.: 2,048,912; 2,334,294; 2,470,796; 2,551,722; 2,792,807; 2,800,875; and 3,516,385.
• Metals, ceramics, glasses, and cermets are used to construct many functional items that are in turn used in carrying out industrial processes. Under certain operating conditions of these processes, surface degradation of a component can result from many causes. These can include the corrosive nature of particular process conditions, thermal effects of the process or environment, contamination from various elements becoming deposited on the surface or infiltrating into the material, deposits formed by catalytic activity between the component's material and the process fluid, galvanic activity between the component's material and the process fluid, concentration cell corrosion, crevice corrosion, graphitic corrosion, and a combination of these degradation mechanisms with each other or with other mechanisms.
• fouling Any kind of degradation is generally referred to as "fouling.”
• the typical solution to these types of fouling is to upgrade the material used to construct the functional item, be it a pipe, a heat exchanger, etc.
• a pipe may be constructed of a nickel alloy stainless steel, rather than of common carbon steel, in an attempt to improve its inner and outer surface longevity and/or functionality.
• tanks used to hold various chemical materials may experience material deposits or reactions on the inner surface of the tank, which can adversely affect the overall process efficiency.
• a heat exchanger may be made from a high nickel content alloy to allow it to withstand high temperature operation (as in the case of a hydrocarbon-fuel gas turbine system) while also reducing the amount of precipitates and deposits that might be occurring due to the caustic environment in which the heat exchanger is required to operate.
• an exhaust valve for use in an internal combustion engine may be made from a particular alloy in an effort to reduce the amount of carbon deposits forming on its surface; carbon deposits are a well known source of operational and emission problems for internal combustion engines.
• crystals of various elements may grow during fluid processing operation because certain exposed molecules within the material surface of the interior of a conduit serve to catalyze the growth of some types of fibers on the interior wall of the conduit.
• carbon fibers grow on the interior of metal pipes used for ethylene transport, petro-chemical cracking tubes, petroleum refinery heaters, natural gas turbine blades, propane and LPG transport tanks, etc. While the mechanism of carbon fiber formation is not entirely clear, it is believed that exposed iron or other atoms at the surface of a steel or iron pipe in, e.g., a petroleum processing facility, may play a role in decomposing hydrocarbons flowing in the pipe into carbon. Because carbon has some solubility in iron, a steel or iron pipe may absorb this carbon.
• amorphous carbon fibers begin to grow rapidly at process temperatures in the range of about 400 0 C to about 800 0 C.
• Such deposits and/or fibrous growths affect the boundary layer development of the fluids and/or vapors passing through the pipe's interior, and can cause a significant restriction in the pipe's ability to transfer fluids, vapors, or slurries.
• a corrosive environment especially due to the presence of water and impurities or salts dissolved in it, causes corrosion of metal pipes leading to eventual failure.
• petrochemical process fluids flowing through a metal tube at high temperature can cause metal wastage in what is known as metal dusting, wherein the tube's inner surface is eroded by various mechanisms.
• methane gas present in the petrochemical stream may react with water to form ice-like structures called hydrates. Hydrate formation in production-stream flow lines in the petroleum industry is also of great concern. Production-stream flow lines carry the raw, produced fluids from the wellhead to a processing facility. If a flow line is operated in the "hydrate region" (i.e., under conditions at which hydrates can form in an oil or gas wellstream), hydrates can deposit on the pipe's inner wall and agglomerate until they completely block the flow line and stop the transport of hydrocarbons to the processing facility.
• hydrate region i.e., under conditions at which hydrates can form in an oil or gas wellstream
• Deposits on the interior surface of a pipe have significant negative impact on the pipe's ability to transfer fluids or gases, and these results can vary depending on the surface roughness of the deposit. For example, a smooth deposit of 5% on the interior of a pipe of circular cross-section can cause a loss of throughput of 10%, and require a pressure increase of 30% to maintain constant flow. An uneven deposit of 5% can increase the loss of throughput to 35% and require a pressure increase of 140% to maintain constant flow. See Cordell, Introduction to Pipeline Pigging, 5 th Edition (ISBN0-901360-33-3).
• Deposit growth on the inside of a pipe can cause deposits or growths to become so large as to nearly stop all fluid flow through the pipe, as shown in Figure 2. Conditions such as these can occur within a few months, or even within a few weeks of operation in the case of certain industrial processes.
• scale is caused by precipitates formed within a process system's enclosures during oil and gas recovery, food processing, water treatment, or other industrial processes.
• the most common scales are inorganic salts such as barium sulphate, strontium sulphate, and calcium carbonate.
• the scales may be partly organic
• Scales formed from sulphates generally are due to mixing of chemically incompatible waters (like sea water and formation water). Carbonate scales result from pressure release of waters containing bicarbonate at high concentration levels. Scaling degrades the process efficiency by plugging sand screens and production pipe, by causing failures in valves, pumps, heat exchangers, and separators. Scaling may also block transportation pipelines.
• combustion buildup known as slag or scale often forms on the flame- heated surfaces of furnaces, boilers, heater tubes, preheaters, and reheaters.
• the degree of combustion buildup depends on the quality of the fuel being burned. Clean natural gas, for example, produces little or no combustion buildup, while coal, a "dirtier" fuel, produces significant combustion buildup.
• coal-fired power plants experience significant combustion buildup on boiler vessels in contact with the coal combustion products. That buildup decreases heat transfer through the surface to the substance being heated, and therefore wastes energy.
• combustion buildup increases the applied temperature necessary to cause the substance to achieve a desired temperature. That increased temperature stresses the boiler vessel, and may lead to material failure. Preventing combustion buildup on the flame-heated surfaces of a fluid transport or processing system would reduce energy consumption and extend equipment lifetime.
• the surfaces exposed to fluid flow may become degraded by the nature of the fluid itself, for example, in the case of hydrogen transport and containment, which has the associated problem of hydrogen embrittlement of the exposed materials.
• sensors detect operational parameters of various processes. By necessity, those sensors inhabit the process material, and are subject to those fouling mechanisms inherent in the processes they monitor. Unfortunately, even the smallest degree of fouling may affect the accuracy of a sensor, even if that same degree of fouling has only a negligible effect on the process itself. Often the remedy to sensor fouling is to design the sensor and sensor mounting apparatus to easily replace fouled sensors. Sensors represent high value components, and frequent sensor replacement adds significant costs in addition to production loss due to shut down for sensor replacement.
• pyrolytic coke When high temperature plays a significant role and forms high molecular weight coke, the resulting material is called pyrolytic coke.
• a metal species such as iron or nickel catalyses the dehydrogenation of a hydrocarbon, leading to what is known as catalytic coking. Elemental carbon then deposits in the metal, weakening it.
• the weakened metal When the system is shut down and cooled for decoking or other maintenance, the weakened metal can crack or spall. In some cases, the carburized metal can spall at process temperatures, resulting in metal dusting mentioned above.
• coke buildup decreases heat transfer, requiring higher process temperatures consuming more energy and lowering equipment lifetime.
• Coke deposits can cause uneven heating, forcing the use of lower temperatures to avoid safety issues. In addition, shutting down those systems to decoke stops production. System shut downs and restarts cause thermal stress and increase the likelihood of system malfunctions and material failure. Reducing coke buildup can extend equipment lifetime, improve process throughput, lower energy consumption and operating temperatures, increase safety, and makes less-expensive alloys available for equipment construction. Moreover, increasing the actual temperature of the process stream (not just the temperature of the outside of the heated vessels) would increase process efficiency and throughput. As it is, many process temperatures are limited by the metallurgy of the heater tubes. Coke buildup requires higher temperatures to be applied outside to obtain a given temperature inside those tubes.
• a second distinct mechanism for fouling equipment in the hydrocarbon industry is corrosion by one or more chemicals present in the process stream.
• hydrogen sulfide (H 2 S) attacks metal surfaces, causing the formation of iron sulfates that flake from hydrocarbon-contacting surfaces, reducing the thickness and strength of process equipment, clogging passages, and potentially diminishing the activity of catalysts downstream.
• ammonia (NH 3 ), ammonium chloride (NH 4 Cl), or hydrogen (H and H 2 ) enhances corrosive attack by H 2 S.
• acids such as hydrochloric acid (HCl), naphthenic acid, sulfuric acid (H 2 SO 4 ), and hydrofluoric acid (HF) cause corrosive attack at various points in hydrocarbon processing systems.
• naphthenic acid corrosion can be observed in process equipment handling diesel and heavier fractions, because naphthenic acids tend to have boiling points similar to diesel fractions.
• Corrosion by sulfuric acid and hydrofluoric acids occurs in alkylating units and associated components employing those acids. Protection against corrosive mechanisms may be found in using chromium, nickel, and molybdenum alloys, and by adding substances to the process stream such as base to neutralize acid.
• H 2 S is added to process streams to reduce metal dusting and other forms of fouling; yet H 2 S itself causes corrosion. That compound also arises during hydrodesulfuring processes, when thiols and other naturally-present organosulfur compounds react to form H 2 S and desulfured hydrocarbons.
• a strong base such as sodium hydroxide or potassium hydroxide in alcohol digests triglycerides and long-chain fatty acids from a biological or renewable source, to form esterified fatty acids (biodiesel) and glycerin.
• That source may be corn, soy, oil palm, pulp, bark, even restaurant waste and garbage.
• the harsh basic environment required for the digestion reaction may cause caustic stress corrosion cracking, also known as caustic embrittlement. Heat treatments and nickel-based alloys may be necessary to avoid cracking, unless a less-expensive or more-effective means can be found to protect that equipment.
• fluid processing or transport system means any equipment within which fluid (used herein to include any material that is wholly or partially in a gaseous or liquid state, and includes, without limitation, liquids, gases, two-phase systems, semi-solid system, slurries, etc.) flows or is stored, such as pipes, tubes, conduits, heat exchangers, beds, tanks, reactors, nozzles, cyclones, silencers, combustion chambers, intake manifolds, exhaust manifolds, ports, etc., as well as any equipment within which a chemical or physical change occurs, wherein at least one of the components participating in the chemical or physical change is a fluid.
• Methods of the invention protect surfaces of such equipment by inhibiting or preventing degradation, irrespective of whether the degradation occurs through deposition of material on the surfaces, through infiltration of material into the surfaces, or through corrosive attack on the material surface.
• the method is adapted to be used, in some embodiments, on fluid process equipment, or portions thereof, after assembly, resulting in significantly decreased interruption or interference with the protective functions of the coating by welds, joints, or other structures within the equipment that are created when the equipment is built or assembled.
• the present invention relates, in some aspects, to forming at least one metal oxide on an interior or exterior surface of fluid transport or process equipment.
• the at least one metal oxide can be formed on the surface by (1) placing at least one metal compound on the surface and (2) converting at least some of the at least one metal compound into at least one metal oxide.
• Metal compounds useful in the present invention contain at least one metal atom and at least one oxygen atom.
• Non-limiting examples of useful metal compounds include metal carboxylates, metal alkoxides, and metal ⁇ -diketonates. Converting the metal compound can be accomplished by a wide variety of methods, such as, for example, heating the environment around the metal compound, heating the substrate under the metal compound, heating the metal compound itself, or a combination of those three.
• converting the metal compound can be accomplished by catalysis.
• Some embodiments of the present invention provide a method for forming at least one metal oxide on a surface of a fluid processing or transport system, or a component thereof, comprising: at least partially assembling the system; applying at least one metal compound to the surface; and exposing the surface with the applied at least one metal compound to an environment that will convert at least some of the compound to at least one metal oxide.
• the fluid processing or transport system is substantially assembled prior to forming at least one metal oxide coating on at least one surface of the system.
• the fluid processing or transport system is fully assembled prior to forming at least one metal oxide coating on at least one surface of the system.
• the invention relates to a method for forming at least one metal oxide on a surface of a fluid processing or transport system, or a component thereof, comprising: applying a metal compound composition to the surface, wherein the metal compound composition comprises at least one metal salt of at least one carboxylic acid; and exposing the surface with the applied metal compound composition to an environment that will convert at least some of the salt to at least one metal oxide.
• the invention relates to a method for forming at least one metal oxide on a surface of a fluid processing or transport system, or a component thereof, comprising: applying a metal compound composition to the surface, wherein the metal compound composition comprises at least one metal alkoxide; and exposing the surface with the applied metal compound composition to an environment that will convert at least some of the metal alkoxide to at least one metal oxide.
• the invention relates to a method for forming at least one metal oxide on a surface of a fluid processing or transport system, or a component thereof, comprising: applying a metal compound composition to the surface, wherein the metal compound composition comprises at least one metal ⁇ -diketonate; and exposing the surface with the applied metal compound composition to an environment that will convert at least some of the metal ⁇ -diketonate to at least one metal oxide.
• the invention relates to a method for forming at least one metal oxide on a surface of a fluid processing or transport system, or a component thereof, comprising: applying a metal compound composition to the surface, wherein the metal compound composition comprises at least one rare earth metal compound, and at least one transition metal compound; and exposing the surface with the applied metal compound composition to an environment that will convert at least some of the compounds to at least one metal oxide
• the at least one metal oxide comprises a metal oxide coating or metal oxide film.
• a metal oxide coating or a metal oxide film in some embodiments, is crystalline, nanocrystalline, amorphous, thin film, or diffuse, or a combination of any of the foregoing.
• a metal oxide coating in some embodiments of the present invention may comprise a film that contains both nanocrystalline and amorphous regions.
• a metal oxide coating or metal oxide film at least partially diffuses or penetrates into surfaces of the fluid processing or transport system thereby precluding any intermediate bonding layers.
• the invention in additional embodiments, relates to a method for forming at least one metal oxide on a surface of a fluid processing or transport system, or a component thereof, comprising: applying a liquid metal compound composition to the surface, wherein the liquid metal compound composition comprises a solution of at least one rare earth metal compound and at least one transition metal compound, in a solvent, and exposing the surface with the applied liquid compound to a heated environment that will convert at least some of the metal compound to at least one metal oxide, thereby forming a metal oxide coating on the surface.
• the metal oxide coating may be crystalline, nanocrystalline, amorphous, thin film, or diffuse, or a combination of any of the foregoing.
• a metal oxide coating in some embodiments of the present invention may comprise a thin film that contains both nanocrystalline and amorphous regions.
• the invention relates to a method for forming an oxidizing coating on an interior surface of a fluid processing or transport system, comprising: applying a liquid metal carboxylate composition to the surface, wherein the liquid metal carboxylate composition comprises a solution of at least one rare earth metal salt of a carboxylic acid and at least one transition metal salt of a carboxylic acid, in a solvent, and exposing the surface with the applied liquid metal carboxylate composition to a heated environment that will convert at least some of the metal carboxylate to metal oxides, thereby forming a thin layer of a nanocrystalline coating on the surface.
• the invention relates to a method for forming an oxidizing coating on an interior surface of a fluid processing or transport system, comprising: applying a liquid metal carboxylate composition to the surface, wherein the liquid metal carboxylate composition comprises a solution of zirconium carboxylate and at least one transition metal salt of a carboxylic acid, in a solvent, and exposing the surface with the applied liquid metal carboxylate composition to a heated environment that will convert at least some of the metal carboxylate to metal oxides, thereby forming a thin layer of a nanocrystalline coating on the surface.
• the method of the invention further includes a step of applying a solution of organosiloxane-silica in ethanol over the formed oxide coating and exposing the coated substrate to an environment that will remove volatile components from the solution without decomposing organo-silicon bonds. In some embodiments, this step can be repeated once or more.
• the various coatings of the present invention are formed, in some embodiments, by a method of forming an oxidizing coating on a substrate comprising:
• liquid metal compound composition comprises a solution of at least one rare earth metal compound and at least one transition metal compound, in a solvent
• the invention relates to metal oxide coatings (and articles coated therewith) containing two or more rare earth metal oxides and at least one transition metal oxide. Further embodiments of the invention relate to metal oxide coatings (and articles coated therewith), containing ceria, a second rare earth metal oxide, and a transition metal oxide. Some embodiments relate to metal oxide coatings (and articles coated therewith), containing yttria, zirconia, and a second rare earth metal oxide. In some cases, the second rare earth metal oxide can include platinum or other known catalytic elements. [0042] In the case of catalytic surfaces, this method allows for cost savings by reducing the bulk amount of the catalyst. And, it also allows a wider variety of catalysts to be applied either as mixtures or in disparate layers to achieve tightly targeted results.
• some embodiments of the invention create a protective metal oxide coating on a chosen surface to serve as a prophylaxis against attack from chemical, thermal, ionic, or electronic degradation.
• the metal oxide coatings of some embodiments prevent the growth of fibers, formation of hydrate crystals, and act as a prophylaxis generally against growth of any materials that block, interfere, or contaminate the successful operation of an enclosed system.
• some embodiments of the present invention provide a method for decreasing or preventing fouling of a surface of a fluid processing or transport system, or a component thereof, comprising applying at least one metal compound to the surface, and exposing the surface with the applied at least one metal compound to an environment that will convert at least some of the compound to at least one metal oxide, wherein the at least one metal oxide is resistant to fouling.
• Other embodiments of the present invention provide a method for decreasing or preventing fouling of a surface of a sensor, or a component thereof, comprising applying at least one metal compound to the surface, and exposing the surface with the applied at least one metal compound to an environment that will convert at least some of the compound to at least one metal oxide, wherein the at least one metal oxide is resistant to fouling.
• Some embodiments of the present invention provide a method for reducing or preventing coke buildup on a surface of a fluid processing or transport system, or a component thereof, comprising applying at least one metal compound to the surface, and exposing the surface with the applied at least one metal compound to an environment that will convert at least some of the compound to at least one metal oxide, wherein the at least one metal oxide is resistant to coke buildup.
• inventions of the present invention provide a method for reducing or preventing corrosive attack on a surface of a fluid processing or transport system, or a component thereof, comprising applying at least one metal compound to the surface, and exposing the surface with the applied at least one metal compound to an environment that will convert at least some of the compound to at least one metal oxide, wherein the at least one metal oxide is resistant to corrosive attack.
• Still other embodiments provide methods for reducing or preventing combustion buildup on a flame-heated surface of a fluid processing or transport system, or a component thereof, comprising: applying at least one metal compound to the surface, and exposing the surface with the applied at least one metal compound to an environment that will convert at least some of the compound to at least one metal oxide, wherein the at least one metal oxide is resistant to combustion buildup.
• Further embodiments provide methods for reducing or preventing fouling of at least one metal surface of a combustion engine system or a component thereof, comprising applying at least one metal compound to the surface, and exposing the surface with the applied at least one metal compound to an environment that will convert at least some of the compound to at least one metal oxide, wherein the at least one metal oxide is resistant to fouling.
• the at least one metal oxide is operable to render a surface of a fluid processing or transport system treated therewith resistant to degradation or fouling for a period of at least days or weeks. In another embodiment, the at least one metal oxide is operable to render a surface of a fluid processing or transport system treated therewith resistant to degradation or fouling for a period of at least months or years. [0051] Some embodiments of the invention provide an improved corrosion-resistant surface treatment through the creation of a nanocrystalline grain structure of zirconia- or cerium- based materials, or surface treatments of other elemental compositions with nanocrystalline microstructures that serve to isolate the substrate from chemical, thermal, or galvanic attack.
• Additional embodiments provide a low cost means to form a useful coating of zirconia- or ceria-based ceramic material on a substrate, the coating having a nanocrystalline microstructure.
• Some embodiments of the technology will prevent electrochemical corrosion by inhibiting the flow of electrons or ions into or from the substrate surface and from or into the process fluid stream.
• Additional embodiments of the invention produce a dense metal oxide coating that does not suffer from cracking due to thermal stresses.
• Some embodiments produce a metal oxide coating that does not suffer from cracking due to its fabrication method.
• the at least one metal oxide coating appears uniform and without cracks or holes from about 10Ox to about 100Ox magnification.
• Some embodiments provide a metal oxide coating comprising only one metal oxide.
• Other embodiments provide a metal oxide coating comprising only two metal oxides.
• Still other embodiments provide a metal oxide coating comprising only three metal oxides.
• the metal oxide coating comprises four or more metal oxides.
• the present invention in some cases, also provides a low cost method for the creation of a metal oxide coating that serves to protect a surface from chemical, thermal, and/or galvanic attack.
• the present invention also provides a means to diffuse chosen surfaces with selected chemical ingredients using a process that does not require damaging high temperature cycles, in several embodiments.
• Yet other embodiments of this invention provide corrosion resistant coatings of organosiloxane-silica over metal oxide coating to impart prolonged usefulness to substrates, when such substrates have the tendency to corrode in aqueous environments with or without salts and other impurities dissolved in water.
• Additional embodiments of the invention provide a means to form a metal oxide coating on the interior of a closed system after it is assembled, giving a prophylactic coating on all surfaces exposed to chosen process including welded areas, flanged joints, etc.
• Some embodiments of this invention provide a process for applying a surface treatment to an interior surface of an industrial process system or a component thereof such that corrosion, erosion, or the building up of debris or a combination thereof is satisfactorily resisted by the surface treatment and the underlying surface, resulting in improved performance of the industrial fluid process system or component thereof.
• Other embodiments of the invention provide a method of forming a metal oxide coating that is well-adhered to chosen interior surfaces of an industrial process system.
• Still other embodiments of the invention provide a method of forming a metal oxide coating on the interior of an enclosed piping system, wherein the coating has a thickness of 5 microns or less.
• Additional embodiments of the invention provide a means to economically form a metal oxide coating to chosen interior surfaces of an industrial process system.
• Yet other embodiments provide a method of forming a metal oxide coating on at least one component of an industrial process system prior to assembly.
• Further embodiments provide a method of forming a metal oxide coating on at least one component of an industrial process system that has been in service, wherein the inner surfaces of the component, for example, a pipe or tube, have been cleaned using any suitable method of cleaning interior surfaces of industrial process system components such as solvent washing, blasting, pigging, etching, mechanical and/or chemical polishing, spalling, steam cleaning, and similar methods.
• Still further embodiments of the invention provide a method of forming a metal oxide coating on at least one portion of an assembled industrial process system so that the welded areas, flanges, and assorted assembly points within the system receive the coating.
• Additional embodiments provide a method of forming a metal oxide coating on at least one portion of an assembled industrial process system after all assembly welding, brazing, and similar joining processes are completed, when so desired, to eliminate the degradation that occurs when components with pre-existing coatings are joined with high temperature joining processes. For example, creating a welded joint on a pipe with a conventional surface treatment typically results in the degradation of the conventional surface treatment in zones adjoining the welded area, greatly reducing or eliminating the effectiveness of the conventional surface treatment.
• Other embodiments of the invention provide a method of forming multiple layers of at least one metal oxide on at least one portion of an assembled industrial process system.
• Some embodiments of the present invention provide a method for forming at least one metal oxide on an interior surface of a fluid processing or transport system or a component thereof, comprising: placing at least one pig proximate to the interior surface; applying at least one metal compound to the interior surface with the at least one pig; and converting at least some of the at least one metal compound to at least one metal oxide.
• the process of placing, applying, and converting can be repeated, forming at least one metal oxide in more than one layer.
• various methods can be used to apply at least one metal compound to the interior surface, in addition to those methods employing at least one pig, again forming at least one metal oxide in more than one layer. Accordingly, in certain embodiments, this invention relates to processes of applying a chosen composition to chosen surfaces of an industrial process system, then utilizing a conversion method to convert the formulation to a useful surface coating.
• At least one metal oxide or metal oxide coating is formed in an inert environment, including an environment wherein no or substantially no oxygen is present. In other embodiments, at least one metal oxide or metal oxide coating is formed in an aerobic environment.
• Industrial fluid processing and/or transport systems operable to be treated with metal oxides including metal oxide coatings include without limitation petroleum refineries, petrochemical processing plants, petroleum transport and storage facilities such as pipelines, oil tankers, fuel transport vehicles, and gas station fuel tanks and pumps, sensors, industrial chemical manufacturing plants, aeronautical and aerospace fluid storage and transport systems including fuel systems and hydraulic systems, food and dairy processing systems, combustion engines, turbine engines, and rocket engines.
• Figure 1 adapted from Figure 6 of U.S. Patent No. 5,230,842, shows a pig assembly useful in some embodiments of the present invention for depositing at least one metal compound on the interior surfaces of a fluid processing or transport system.
• Figure 2 shows a photograph of a cross section of an untreated pipe revealing crystalline growth that restricts flow through the pipe.
• Figure 3 shows a photograph of an uncoated steel coupon after a one hour exposure to Aqua Regia.
• Figure 4 shows a photograph of a steel coupon coated with "Zircon” after one hour exposed to Aqua Regia.
• Figure 5 shows a photograph of a steel coupon coated with "Glass” after one hour exposed to Aqua Regia.
• Figure 6 shows a photograph of a steel coupon coated with "YSZ" after one hour exposed to Aqua Regia.
• Figure 7 shows a photograph of a steel coupon coated with "Clay" after one hour exposed to Aqua Regia.
• Figure 8 shows TEM micrograph at approximately two million x magnification of a steel substrate having a Y/Zr oxide coating in cross-section.
• the term "rare earth metal” includes those metals in the lanthanide series of the Periodic Table, including lanthanum.
• the term “transition metal” includes metals in Groups 3-12 of the Periodic Table (but excludes rare earth metals).
• the term “metal oxide” particularly as used in conjunction with the above terms includes any oxide that can form or be prepared from the metal, irrespective of whether it is naturally occurring or not.
• the "metal” atoms of the metal oxides of the present invention are not necessarily limited to those elements that readily form metallic phases in the pure form.
• Metal compounds include substances such as molecules comprising at least one metal atom and at least one oxygen atom. Metal compounds can be converted into metal oxides by exposure to a suitable environment for a suitable amount of time.
• phase deposition includes any coating process onto a substrate that is subsequently followed by the exposure of the substrate and/or the coating material to an environment that causes a phase change in either the coating material, one or more components of the coating material, or of the substrate itself.
• a phase change may be a physical phase change, such as for example, a change from fluid to solid, or from one crystal phase to another, or from amorphous to crystalline or vice versa.
• Adaptable to provide indicates the ability to make available.
• an “article adaptable to provide a surface in a fluid processing or transport system” is an article, such as a pipe, that has a surface that is or can be assembled into such a system by using manufacturing, construction, and/or assembly steps.
• a device commonly known as a "pig” is used.
• a pig comprises any suitable features and characteristics.
• a pig comprises a body, and optionally one or more brushes, spray nozzles, absorbent structures such as polymer foams and sponges, stabilizers, hydraulic cups, hydraulically-driven wheels and/or tracks, mechanically-driven wheels and/or tracks, conversion devices such as IR emitters, and the like.
• the pig can act to distribute the at least one metal compound onto the surface to be treated.
• the pig acts as a mobile plug, containing a volume of the at least one metal compound, thereby distributing it to the surface.
• the pig acts as a mobile converter, causing at least some of the at least one metal compound to convert to at least one metal oxide.
• a pig is or comprises a sponge.
• Suitable sponges include, but are not limited to, open cell foams, closed cell foams, sponges having a diameter greater than the interior diameter of a pipe to be treated, and sponges comprising polyurethane, polyester, polyethylene, polyvinyl alcohol, cellulose, natural sponge, and combinations thereof. It is customary to use pigs that are fairly dense and relatively uncompressible, and having a diameter that is perhaps five percent larger than the interior diameter of a pipe to be treated with the pig. However, if that pig is damaged during its passage through a pipe, the pig could loose its ability to form a seal sufficient to allow the pig to be pushed through the pipe. Applicants have unexpectedly found that using a highly compressible sponge as the pig affords numerous advantages over less-compressible pigs. Some of those advantages, one or more of which might be present in a given embodiment of the present invention, include:
• Highly compressible sponges are better able to maneuver through "mule ears," which are 90 degree intersections of one pipe entering another, and other difficult pipe geometries such as elbows and U-bends.
• a compressible sponge can navigate a U-bend that appears very close to the pig launching flange, whereas a rigid pig cannot build the momentum necessary to get past the U-bend. Rigid pigs frequently get stuck and destroyed navigating difficult pipe geometries.
• Highly compressible sponges can treat pipes having different internal diameters. A less-compressible pig passing from a narrower diameter to a larger diameter might loose its ability to form a seal, and may become stuck in the wider portion of the pipe.
• a highly compressible sponge having substantial "deflection” or resiliency can expand to fully contact and treat the entire inner surface of the wider portion of the pipe, and is less likely to loose its seal.
• a highly compressible sponge such as an open cell foam sponge, can absorb a treating liquid, and then apply that liquid to the inner surface of a pipe.
• a non-compressible pig requires a quantity of treating liquid to be placed in the pipe before the pig. That can be messy, or it can require more than one pig to contain the treating liquid.
• a sponge need not have a particular shape, whereas a pig is usually manufactured to have a certain shape to travel through a pipe. This advantage allows costs savings, in addition to the greater maneuverability mentioned above.
• a pigging package comprising a first pig and a second pig, and a quantity of coating liquid that comprises at least one metal compound.
• Further embodiments comprise one or more additional pigs or other components positioned between the first pig and the second pig.
• the first pig acts as a sealing element within a pipe or tube and a second pig is positioned within a chosen section of a pipe at a distance rearward of the first pig such that a volume is defined by the aft section of the first pig, the inner walls of the pipe, and the front segment of the second pig.
• This defined volume may be filled with the coating liquid and the second pig constructed such that as the pair of pigs is transported through the pipe, a thin film of liquid is allowed to leak past the trailing (second) pig and thus the liquid becomes distributed on the inner surface of the pipe.
• the trailing pig may be constructed with an outer surface being comprised of an absorbent material, for example, urethane foam, such that the trailing (second) pig serves as a swab that applies the liquid to the inner surface of the pipes inner walls.
• the volume of liquid that resides between the first pig and the second pig serves as a reservoir to keep the trailing pig saturated with the liquid formulation such that the wetting of the inner surface of the pipe's inner walls is accomplished in a continual fashion for a chosen length within the pipe.
• the motive force for the movement of the pigging package may be provided by air or other gas pressure provided behind the trailing pig, taking advantage of the fact that the coating liquid residing between the two pigs is an incompressible liquid and thus the gas pressure acting upon the trailing (second) pig will be transferred to the leading (first) pig and, provided that the gas pressure ahead of the leading (first) pig is sufficiently lower than the gas pressure pressing on the backside of the trailing (second) pig, movement will occur as the pigging package moves toward the zone within the pipe with lower gas pressure.
• gas pressure pressing against the trailing pig may need to be greater than the gas pressure ahead of the leading pig by a value of up to 600 psi in some cases to promote movement of the pigging package.
• gas pressure may be supplied using any suitable methods, such as, for example, one or more of compressors, fans, pumps, chemical reactions, combustion, and the like.
• the motive force for the pigging package may be provided by compressed inert gas or gaseous mixture such that the wetted inner surfaces of the piping system are at least partially prevented from oxidizing once wetted with the coating liquid.
• the inert gas or gaseous mixture may be heated to a chosen temperature sufficient to convert at least a portion of the coating liquid wetting the pipe's inner surfaces into a metal oxide coating.
• an inert gas may be fed into the piping system after it has been wetted with the coating liquid but prior to heating of even a portion of the pipe walls. The inert gas, in some embodiments, controls oxidation of the wetted pipe surfaces as their temperature is increased.
• the motive force for the pigging package may be provided by hydraulic pressure provided to the rearmost sections of the trailing pig, said hydraulic pressure being sufficiently higher than the pressure, whether gas or hydraulic, that exists ahead of the leading pig, and thus promoting the desired motion in the pigging package.
• the frictional forces that exist between the pigs and the inner walls of the pipe will determine the amount of pressure, either gaseous or hydraulic, that will be needed to move the pigging package through the pipe at the desired rate.
• a spray head may be provided in one or both of the pigs through which the coating material may be applied to the inner surface of the pipe.
• the pressure required to discharge the coating material may be provided by a pressure container provided in the pigging package as taught in U.S. Patent No. 4,774,905, which is incorporated by reference in its entirety.
• the pressure required to discharge the coating material may be provided by the motive pressure, whether hydraulic or gaseous, that may be used to push the pigging package through the piping system.
• the motive pressure that is acting upon the trailing pig will be physically transferred by default to the coating material residing between the two pigging elements, thus pressurizing the liquid coating material within this defined reservoir. This pressure may be used to force the liquid coating material through one or more spray nozzles to apply the coating material to the inner surfaces of the pipe.
• a known pressure regulator may be provided between the pressurized coating material reservoir and the spray head(s) that limits the liquid feed pressure to the spray head to a desired level, for example, 100 psi.
• the liquid coating material may be provided by a feed line connected to one of the pigging elements such that one or both pigging elements remain saturated with the liquid coating material and a desired amount of liquid is dispersed onto the inner surface of the pipe.
• the feed line may have guide discs provided along its length to prevent the line from touching the inner surfaces of the pipe and thus restricting the line's movement.
• the liquid coating material may be provided by a feed line connected to one of the pigging elements such that at least one spray nozzle provided with the pig assembly may receive a sufficient supply of the coating liquid to disperse a desired amount of liquid onto the chosen surfaces of the pipe.
• the pressurized liquid coating material may be provided by a feed line connected to at least one pig provided with a spray nozzle for the application of the liquid coating material to chosen surfaces of an industrial process system wherein the motive force for movement of the pigging device is provided by a hydraulic actuator motor driving traction devices such as wheels, said actuator capturing a portion of the feed line liquid pressure prior to the coating material being sprayed from the provided spray nozzle, said hydraulic pressure being provided upstream at the head of the feed line via known means such as pumps, compressors, or similar.
• the pressure that is used to feed the spray nozzle is interrupted prior to being ejected from the nozzle and its pressure energy is used to drive the pig forward using wheels driven by a hydraulic motor.
• a single pig may be pulled through a pipe by a feed line that transfers sufficient liquid coating material to the pig such that the pig's absorbent material remains saturated to a level that leaves a well-wetted surface on the inside of the pipe, said feed line also being sufficiently strong to provide the necessary pulling force to move the pig through the pipe or piping system.
• a single pig may be pulled through a pipe by a feed line that transfers sufficient liquid coating material to the pig and feeds a spray device provided in the pig that atomizes the liquid coating material and directs it to the inside of the pipe, said feed line also being sufficiently strong to provide the necessary pulling force to move the pig through the pipe or piping system.
• guides may be provided at chosen points along the feed tube to keep the feed tube centered within the cross sectional plane of the pipe.
• the guides that center the feed tube may be constructed using known spring steel guides, rigid discs, or other means known to those skilled in the art.
• the liquid coating comprising at least one metal compound may be applied to the inner surface of a pipe and then exposing the wetted surface to an environment that will convert at least some of the compound to at least one metal oxide, for example, through the elevation of the temperature of the wetted surface to a desired temperature through known means.
• alkyl refers to a saturated straight, branched, or cyclic hydrocarbon, or a combination thereof, including Cj to C 24 , methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, t-butyl, n-pentyl, cyclopentyl, isopentyl, neopentyl, n-hexyl, isohexyl, cyclohexyl, 3-methylpentyl, 2,2-dimethylbutyl, 2,3-dimethylbutyl, heptyl, octyl, nonyl, and decyl.
• alkoxy refers to a saturated straight, branched, or cyclic hydrocarbon, or a combination thereof, including Ci to C 24 , methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, t-butyl, n-pentyl, cyclopentyl, isopentyl, neopentyl, n-hexyl, isohexyl, cyclohexyl, 3-methylpentyl, 2,2-dimethylbutyl, 2,3-dimethylbutyl, heptyl, octyl, nonyl, and decyl, in which the hydrocarbon contains a single-bonded oxygen atom that can bond to or is bonded to another atom or molecule.
• alkenyl and alkynyl refer to straight, branched, or cyclic hydrocarbon with at least one double or triple bond, respectively.
• Alkenyl and alkynyl include, but are not limited to, Ci to C 24 hydrocarbons.
• aryl or aromatic refers to monocyclic or bicyclic hydrocarbon ring molecule having conjugated double bonds about the ring.
• the ring molecule has 5- to 12-members, but is not limited thereto.
• the ring may be unsubstituted or substituted having one or more alike or different independently- chosen substituents, wherein the substituents are chosen from alkyl, alkenyl, alkynyl, alkoxy, hydroxyl, and amino radicals, and halogen atoms.
• Aryl includes, for example, unsubstituted or substituted phenyl and unsubstituted or substituted naphthyl.
• the ring molecule has 5- to 12-members, but is not limited thereto.
• hydrocarbon refers to molecules that contain carbon and hydrogen.
• Suitable metal compounds that form metal oxides include substances such as molecules containing at least one metal atom and at least one oxygen atom.
• metal compounds that form metal oxides include metal carboxylates, metal alkoxides, and metal ⁇ -diketonates.
• the metal salts of carboxylic acids useful in the present invention can be made from any suitable carboxylic acids according to methods known in the art.
• U.S. Patent No. 5,952,769 to Budaragin discloses suitable carboxylic acids and methods of making metal salts of carboxylic acids, among other places, at columns 5-6.
• the disclosure of U.S. Patent No. 5,952,769 is incorporated herein by reference.
• the metal carboxylate can be chosen from metal salts of 2-hexanoic acid.
• suitable metal carboxylates can be purchased from chemical supply companies.
• cerium(III) 2- ethylhexanoate, magnesium(II) stearate, manganese(II) cyclohexanebutyrate, and zinc(II) methacrylate are available from Sigma-Aldrich of St. Louis, MO. See Aldrich Catalogue, 2005-2006. Additional metal carboxylates are available from, for example, Alfa-Aesar of Ward Hill, MA.
• the metal carboxylate composition in some embodiments of the present invention, comprises one or more metal salts of one or more carboxylic acids ("metal carboxylate").
• Metal carboxylates suitable for use in the present invention include at least one metal atom and at least one carboxylate radical -OC(O)R bonded to the at least one metal atom.
• metal carboxylates can be produced by a variety of methods known to one skilled in the art. Non-limiting examples of methods for producing the metal carboxylate are shown in the following reaction schemes: nRCOOH + Me ⁇ (RCOO) n Me 0+ + 0.5nH 2 (for alkaline earth metals, alkali metals, and thallium).
• nRCOOH + Me n+ (0H) n ⁇ (RCOO) n Me 0+ + nH 2 0 for practically all metals having a solid hydroxide.
• X is an anion having a negative charge m, such as, e.g., halide anion, sulfate anion, carbonate anion, phosphate anion, among others; n is a positive integer; and Me represents a metal atom.
• R in the foregoing reaction schemes can be chosen from a wide variety of radicals.
• Suitable carboxylic acids for use in making metal carboxylates include, for example: Monocarboxylic acids:
• R is hydrogen or unbranched hydrocarbon radical, such as, for example, HCOOH - formic, CH 3 COOH - acetic, CH 3 CH 2 COOH - propionic, CH 3 CH 2 CH 2 COOH (C 4 H 8 O 2 )- butyric, C 5 H 10 O 2 - valeric, C 6 H 12 O 2 - caproic, C 7 H 14 - enanthic; further: caprylic, pelargonic, undecanoic, dodecanoic, tridecylic, myristic, pentadecylic, palmitic, margaric, stearic, and nonadecylic acids;
• R is a branched hydrocarbon radical, such as, for example, (CH 3 ) 2 CHCOOH - isobutyric, (CH 3 ) 2 CHCH 2 COOH - 3-methylbutanoic, (CH 3 ) 3 CCOOH - trimethylacetic, including VERSATIC 10 (trade name) which is a mixture of synthetic, saturated carboxylic acid isomers, derived from a highly-branched C 10 structure;
• R is a branched or unbranched hydrocarbon radical that contains one hydroxyl substituent, such as, for example, HOCH 2 COOH - glycolic, CH 3 CHOHCOOH - lactic, C 6 H 5 CHOHCOOH - amygdalic, and 2-hydroxybutyric acids;
• Dioxycarboxylic acids in which R is a branched or unbranched hydrocarbon radical that contains two oxygen atoms each bonded to two adjacent carbon atoms, such as, for example, C 6 H 3 (OH) 2 COOH - dihydroxy benzoic, C 6 H 2 (CH 3 )(OH) 2 COOH - orsellinic; further: caffeic, and piperic acids;
• R is a branched or unbranched hydrocarbon radical that contains one aldehyde group, such as, for example, CHOCOOH - glyoxalic acid
• Monoaromatic carboxylic acids in which R is a branched or unbranched hydrocarbon radical that contains one aryl substituent, such as, for example, C 6 H 5 COOH - benzoic, C 6 H 5 CH 2 COOH - phenylacetic, C 6 H 5 CH(CH 3 )COOH -
• R is a branched or unbranched hydrocarbon radical that contains at least one carboxylic acid group, such as, for example, ethylene diamine N,N'-diacetic acid, and ethylene diamine tetraacetic acid (EDTA);
• R is a branched or unbranched hydrocarbon radical containing at least one hydroxyl substituent and at least one carboxylic acid group, such as, for example, HOOC-CHOH-COOH - tartronic,
• the monocarboxylic acid comprises one or more carboxylic acids having the formula I below: R°-C(R")(R') ⁇ C00H (I) wherein:
• R° is selected from H or C 1 to C 24 alkyl groups
• R and R" are each independently selected from H and Ci to C 24 alkyl groups; wherein the alkyl groups of R°, R, and R" are optionally and independently substituted with one or more substituents, which are alike or different, chosen from hydroxy, alkoxy, amino, and aryl radicals, and halogen atoms.
• Some suitable alpha branched carboxylic acids typically have an average molecular weight in the range 130 to 420. In some embodiments, the carboxylic acids have an average molecular weight in the range 220 to 270.
• the carboxylic acid may also be a mixture of tertiary and quaternary carboxylic acids of formula I. VIK acids can be used as well. See U.S. Patent No. 5,952,769, at col. 6, 11. 12-51.
• Either a single carboxylic acid or a mixture of carboxylic acids can be used to form the metal carboxylate composition.
• a mixture of carboxylic acids is used.
• the mixture contains 2-ethylhexanoic acid where R° is H, R" is C 2 H 5 and R' is C 4 Hg in formula (I) above.
• this acid is the lowest boiling acid constituent in the mixture.
• the mixture has a broader evaporation temperature range, making it more likely that the evaporation temperature of the mixture will overlap the metal carboxylate decomposition temperature, allowing the formation of a solid metal oxide coating.
• the possibility of using a mixture of carboxylates avoids the need and expense of purifying an individual carboxylic acid.
• any of the aforementioned carboxylic acids may be suitable, alone or in combination.
• Metal alkoxides suitable for use in the present invention include at least one metal atom and at least one alkoxide radical -OR 2 bonded to the at least one metal atom.
• Such metal alkoxides include those of formula II:
• R 2 can be alike or different and are independently chosen from unsubstituted and substituted alkyl, unsubstituted and substituted alkenyl, unsubstituted and substituted alkynyl, unsubstituted and substituted heteroaryl, and unsubstituted and substituted aryl radicals, wherein substituted alkyl, alkenyl, alkynyl, heteroaryl, and aryl radicals are substituted with one or more alike or different substituents independently chosen from halogen, hydroxy, alkoxy, amino, heteroaryl, and aryl radicals.
• z is chosen from 2, 3, and 4.
• Metal alkoxides are available from Alfa-Aesar and Gelest, Inc., of Morrisville,
• metal alkoxides useful in embodiments of the present invention include methoxides, ethoxides, propoxides, isopropoxides, and butoxides and isomers thereof.
• the alkoxide substituents on a give metal atom are the same or different.
• metal dimethoxide diethoxide, metal methoxide diisopropoxide t-butoxide, and similar metal alkoxides can be used.
• Suitable alkoxide substituents also may be chosen from:
• Aliphatic series alcohols from methyl to dodecyl including branched and isostructured.
• Aromatic series alcohols benzyl alcohol - C 6 H 5 CH 2 OH; phenyl-ethyl alcohol - C 8 H 10 O; phenyl- propyl alcohol - CgH 12 O, and so on.
• Metal alkoxides useful in the present invention can be made according to many methods known in the art.
• One method includes converting the metal halide to the metal alkoxide in the presence of the alcohol and its corresponding base. For example:
• Metal ⁇ -diketonates suitable for use in the present invention contain at least one metal atom and at least one ⁇ -diketone of formula III as a ligand:
• R 3 , R 4 , R 5 , and R 6 are alike or different, and are independently chosen from hydrogen, unsubstituted and substituted alkyl, unsubstituted and substituted alkoxy, unsubstituted and substituted alkenyl, unsubstituted and substituted alkynyl, unsubstituted and substituted heteroaryl, unsubstituted and substituted aryl, carboxylic acid groups, ester groups having unsubstituted and substituted alkyl, and combinations thereof, wherein substituted alkyl, alkoxy, alkenyl, alkynyl, heteroaryl, and aryl radicals are substituted with one or more alike or different substituents independently chosen from halogen atoms, hydroxy, alkoxy, amino, heteroaryl, and aryl radicals.
• the ⁇ -diketone of formula III may assume different isomeric and electronic configurations before and while chelated to the metal atom.
• the free ⁇ -diketone may exhibit enolate isomerism.
• the ⁇ -diketone may not retain strict carbon-oxygen double bonds when the molecule is bound to the metal atom.
• Examples of ⁇ -diketones useful in embodiments of the present invention include acetylacetone, trifluoroacetylacetone, hexafluoroacetylacetone, 2,2,6,6-tetramethyl- 3,5-heptanedione, 6,6,7,7,8, 8, 8-heptafluoro-2,2-dimethyl-3,5-octanedione, ethyl acetoacetate, 2-methoxyethyl acetoacetate, benzoyltrifluoroacetone, pivaloyltrifluoroacetone, benzoyl- pyruvic acid, and methyl-2,4-dioxo-4-phenylbutanoate.
• ligands are possible on the metal ⁇ -diketonates useful in the present invention, such as, for example, alkoxides such as -OR 2 as defined above, and dienyl radicals such as, for example, 1,5-cyclooctadiene and norbornadiene.
• Metal ⁇ -diketonates useful in the present invention can be made according to any method known in the art. ⁇ -diketones are well known as chelating agents for metals, facilitating synthesis of the diketonate from readily available metal salts. [00145] Metal ⁇ -diketonates are available from Alfa- Aesar and Gelest, Inc. Also,
• ports may be provided within the exterior surfaces of an enclosed component of an industrial system, for example, in the wall of a pipe, said ports providing a means for delivery of a liquid wherein the pressure within the pipe to be coated is lowered to a sufficient level to produce at least partial vaporization of the liquid as it is delivered to the interior portions of the pipe, such that the vaporized portion of the liquid then condenses on the inner surfaces of the pipe and provides a well- wetted surface.
• multiple delivery ports for delivering the liquid coating material into the low pressure interior of a pipe may be provided along a length of pipe, for example, and a chosen fluid delivered to each port via known manifolds, piping, or other fluid transfer means such that sufficient liquid material is delivered to the interior of the pipe and partially or fully vaporized wherein the condensation of the coating material vapors onto the inner surfaces of the pipe to establish a desired coating on the interior surfaces of the pipe.
• existing holes provided within a system for thermocouple placement may be used, temporarily or permanently, as introduction ports through which a coating material may be introduced to the interior of a sealed system, said coating material subsequently being at least partially vaporized via a reduction in pressure within the sealed system.
• wetting of the inner surfaces of the pipe is followed by a curing phase wherein heat is provided to the surfaces using suitable methods to achieve the conversion of at least a portion of the delivered liquid into a metal oxide coating.
• suitable methods for converting at least a portion of the at least one metal compound into at least one metal oxide include, but are not limited to, flushing the wetted system or component thereof with high-temperature gas; induction heating of the walls of the system or component; heating with one or more lasers, microwave emitters, infrared emitters, or plasma; flaming, for example of the outside walls of the system or component, exposing the wetted system or component to the thermal energy of one or more exothermic reactions, and combinations thereof.
• a flexible feed tube may be provided along the inside of a pipe wherein the feed tube has small holes provided within its exterior leading to its interior such that when the pressure within the tube is higher than the pressure outside of the tube, fluid or gases within the tube are caused to move from within the feed tube to the interstitial space between the tube's outer surface and the pipe's inner surface such that at least a portion of the fluid condenses onto the inner surface of the pipe.
• the pressure within the interstitial space between the flexible tube and the inner wall of the pipe may be provided with a sufficient vacuum level such that any liquid within the flexible tube will be drawn into the interstitial space and subsequently deposit on the inner surfaces of the pipe.
• a coating may be formed on the inside of a pipe or passageway through the use of a spray nozzle fed by a flexible hose.
• a composition comprising at least one metal compound is supplied at sufficient pressure to achieve a uniform application of the composition on the inner surfaces of the passageway, such as by dispersion through one or more spray nozzles affixed to at least one pig.
• the at least one metal compound may be converted to a coating on the inner surfaces of the passageway through a heating process provided by an infrared emitter that is placed into the passageway proximate to the wetted area.
• At least one IR emitter is mounted to a pig that also supports a spray nozzle and a means to keep the spray nozzle and IR emitter centered within the passageway.
• Such means comprises, in some embodiments, guides such as flexible fingers or other suitable structures for centering devices within passageways, such as those familiar to persons skilled in the art.
• the at least one IR emitter is located downstream of the spray nozzle such that the spray droplets of the composition are fully dispersed and in contact with the passageway's inner wall prior to the IR emitter's electromagnetic radiation being proximate to the surface and thus providing a means to reduce the amount of airborne spray that might contact the IR emitter itself.
• the at least one IR emitter is located on the same pig as one or more spray nozzles. In other embodiments, the at least one IR emitter is located on a pig other than the pig comprising one or more spray nozzles.
• a feed of an inert gas may be provided to create a non- oxidizing atmosphere for the heating process of the conversion liquid and the material underneath such that oxidation of the inner wall of the passageway is reduced or eliminated.
• the spray nozzle is fed with liquid under pressure through a flexible line, the IR emitter is supplied with electrical power via suitable electrical wires.
• the guides and spray nozzle(s) may be located upstream of the IR emitter and the liquid feed may be supplied by a pipe or tube that extends away from the assembly through the pipe system and out to a reservoir with a fluid pump and may also have an electrical supply wire that extends away from the assembly through the pipe system and out to an electrical supply suitable for the power requirements of the IR emitter and any other devices mounted to the assembly.
• a liquid composition comprising at least one metal compound may be applied to the selected surfaces of a fluid flow system using a motorized pig that is equipped with at least one spray nozzle and one or more traction drive devices wherein the motorized pig is moved through a piping system and sprays the composition on the insides of the pipe.
• the composition can be supplied via a reservoir provided within the pig assembly.
• Means of providing pressure to the spray head is also provided using known means such as stored air pressure, electric pumps, or similar, and the motive force for the traction drive is provided using stored air pressure, electric pumps, or similar.
• the pig would travel in a chosen direction with the spray head being at its rearward end, thus leaving an uninterrupted liquid application of the composition on the chosen surfaces of the piping system as it traveled.
• the pig may be moved via a tether or cable attached to the pig assembly at a chosen point.
• the motive power to move the pig assembly through the system to apply a composition to the interior surfaces of the passage way(s) may be provided by tension applied to the liquid feed lines, electrical supply wires, a separate cable of sufficient strength to pull the assembly, or a combination thereof.
• the tension is provided by known means, in some embodiments, such as an electric motor driven reel device mounted outside the piping system and controlled through known means to provide a desired speed of travel of the pig assembly while simultaneously providing the liquid coating material at a desired delivery rate through the feed line and providing any necessary electrical current flow at a chosen voltage through optional electrical feed wires that run from the reel device to the assembly.
• known means such as an electric motor driven reel device mounted outside the piping system and controlled through known means to provide a desired speed of travel of the pig assembly while simultaneously providing the liquid coating material at a desired delivery rate through the feed line and providing any necessary electrical current flow at a chosen voltage through optional electrical feed wires that run from the reel device to the assembly.
• the coating assembly may first move to a chosen location within a pipe, passageway, or piping system through the use of gaseous pressure acting against a pigging device attached to the coating assembly such that the pigging device acts as a partial or full plug to the pipe's cross section and, when pressure is applied to the interior of the pipe upstream of the pigging device, the difference in pressure between the upstream portions and the downstream portions with respect to the pigging device cause its movement toward the lower pressure zone.
• the pigging device and the attached coating assembly which may incorporate guides, spray nozzle, and IR emitter, or a combination thereof, may be moved to a chosen location within the piping system and then retracted using tension provided onto at least one of the feed lines or wires.
• a vaporization phase created after the liquid coating material is applied to the inner surfaces of the pipe wherein the wetted surfaces are exposed to an ambient pressure near to or lower than the vapor pressure of the liquid coating material, resulting in at least some of the liquid coating material to change from the liquid phase to the vapor phase, followed by a rise in absolute pressure within the system causing at least a portion of the vaporous phase coating material to condense on at least some of the inner surfaces of the pipe, said process greatly aiding the even distribution of the coating material over the inner surfaces of the pipe.
• the vaporization of at least some of the liquid coating material may be achieved through the use of a vacuum pump system that is fluidically connected to the interior volume of a pipe system and allowed to evacuate the interior volume created by the inner surfaces of the pipe and corresponding seals or plugs that may be provided at any open ends or ports within the piping system.
• the reduction in local pressure within the interior of a piping system and its full or partial restoration to ambient pressure may be achieved through known control systems using one or more vacuum pumps, or through the use of ports and valves operated through manual, semi-automatic, or automatic means known to those skilled in the art of industrial process control.
• the required vacuum may be provided by any one of a variety of known vacuum-producing systems including, but not limited to, pumps, blowers, molecular drag systems, turbo-molecular systems, cryosorption processes, sputter-ion pump, and similar.
• the reduction in pressure within the pipe's interior may be provided through a reduction in temperature of the piping system while the system is completely sealed, taking advantage of the natural reduction in pressure and volume that will occur as a sealed system is allowed to cool and the internal gases contract in accordance with the Ideal Gas Law, expressed as
• the high temperature used to convert the liquid coating material to a useable surface treatment may also be used to create the required vacuum for dispersion of the next cycle of coating application by first heating the piping system using a suitable heating means, for example, a furnace, then sealing the pipe ends and any ports, trapping ambient air inside of the pipe along its length, then allowing the pipe and contained air to cool to a desired temperature wherein the contraction of the air trapped inside the sealed pipe would cause the pressure to drop to desired levels, then the introduction of a liquid coating material through chosen ports or passageways would result in the liquid's vaporization.
• additional evacuation may be necessary to achieve the desired vacuum levels.
• the low pressure that develops within the sealed pipe system may need to be bled off to prevent the pressure level from decreasing below a chosen level which might cause unwanted stresses or other vacuum-related problems to be imposed upon the piping system.
• the pipe may be filled with a chosen gas, such as an inert gas, prior to the sealing and cooling operation so that the liquid coating material, once introduced into the pipe system, will be vaporized in an atmosphere other than normal air inside the pipe.
• an inert gas as an example, nitrogen
• nitrogen may be used to completely or partially fill the pipe, and would provide an inert atmosphere for the vaporization of the liquid coating material such that the subsequent heating operation results in the conversion of the liquid matter into a coating with the desired characteristics.
• a reducing gas such as hydrogen may be introduced into the piping system prior to cooling and injection of the liquid coating material such that the subsequent heating operation results in the conversion of the liquid matter into a coating with desired characteristics.
• the heating process may be achieved using known methods such as external heating via induction, internal heating using flow gases or liquids at chosen temperatures, via microwave emissions, via flame impingement on the exterior or interior of the system, and similar methods.
• a piping system may be coated through the use of vapor deposition of a coating material by first sealing off a chosen segment of a piping system or component, then evacuating the inner volume of the sealed piping system to a chosen level of vacuum, then by the introduction of a liquid formulation comprised of the desired coating material, said liquid formulation becoming vaporized as it is introduced into the evacuated inner volume of the piping system wherein sufficient liquid is allowed to pass into the inner volume of the piping system to achieve full or partial saturation of the gases remaining in the inner volume, then, through the introduction of a chosen gas, for example, nitrogen, the pressure within the sealed piping system is allowed to rise to a chosen level, resulting in the condensation of the vapor phase coating material into liquid phase coating material, said condensation resulting in the even wetting of the interior surfaces of the sealed system.
• a chosen gas for example, nitrogen
• the condensation process if followed by the heating of these wetted surfaces to a temperature sufficient to convert at least a portion of the at least one metal compound into at least one metal oxide coating.
• multiple layers of similar or differing metal oxide coatings may be achieved using repeated cycles of the vaporization and condensation process described above.
• additional layers of coating material may be applied to a chosen surface using a combination of known methods to achieve the desired final coating construction, for example, spraying on at least one metal compound and then converting it to at least one metal oxide may be followed by vapor deposition of a subsequent film which may be followed by additional layers using a chosen application method described within this application or using an alternate method as desired.
• the method of the invention can include a pre- application cleaning step prior to the application of the composition.
• the invention involves the application of one or more cleaning materials, which may be in vapor, liquid, semi-solid phase, or a combination of these to at least a portion of the surfaces of the final system, followed by a flushing and drying cycle at a drying temperature.
• the cleaning technique can be of the type used for cleaning surfaces prior to coating, plating, painting, or similar surface treatments.
• the pre-application cleaning step may also include a pickling operation using known chemicals and process in order to prepare the surface(s) for coating.
• Certain embodiments employ a cleaning composition that comprises one or more acids.
• Other embodiments employ a cleaning composition that comprises one or more carboxylic acids.
• one or more pigs contact a cleaning composition and is placed into launching communication with the pipe to be treated. Then the pig(s) is driven through the pipe, allowing the cleaning composition to contact, and thereby clean, the interior of the pipe.
• the same or different pigs can pass through the pipe more than once, contacting the interior surface of the pipe with the same or different cleaning composition.
• a first cleaning composition could be an acid
• a second cleaning composition could be water or a mild base to neutralize the acid.
• the cleaning composition(s) is removed by any suitable method, such as, for example, flushing with fluid such as water, dry air, and/or nitrogen, and/or by heating the environment inside the pipe to drive off the cleaning composition(s).
• the environment inside the pipe contacted with a cleaning composition is heated to about 400 °C to about 427 0 C in the presence of nitrogen, cooled, and flushed with nitrogen or dry air. Heating can be done in the presence of nitrogen, in certain cases, to limit the reaction of the surface with oxygen and/or water at the heating temperature.
• the cleaning composition is substantially removed when any remaining amount or residue would not interfere with the use of the pipe or the further treatment (such as forming a metal oxide) of the pipe.
• spherical sponges are soaked with a cleaning composition and individually passed through a pipe to be cleaned and removed at the other end of the pipe, driven by compressed air. After one, two, three, four or more passes, the pipe is sealed, flushed with nitrogen, and heated to remove the cleaning composition. Upon cooling, the pipe can be cleaned further, or a coating composition can contact the interior of the pipe in accordance with other embodiments of the present invention disclosed herein.
• some embodiments provide a method for cleaning the interior surface of a pipe, comprising: placing a first pig proximate to the interior surface of the pipe, wherein the first pig is a compressible sponge having a diameter in an uncompressed state at least about 1.4 times the largest inner diameter of the pipe; applying a first cleaning composition to the interior surface with the first pig, thereby cleaning the interior surface, wherein the first cleaning composition comprises a carboxylic acid; and substantially removing the first cleaning composition from the interior surface.
• the foregoing method further comprises, before substantially removing the first cleaning composition, placing a second pig proximate to the interior surface of the pipe; and applying a second cleaning composition to the interior surface with the second pig, wherein substantially removing the first cleaning composition also substantially removes the second cleaning composition.
• the diameter in this case, refers to the diameter relative to the cross section of the pipe to be treated.
• an oblong or bullet shaped pig has a diameter relative to the pipe's inner diameter, considering the orientation the pig will adopt inside the pipe.
• the diameter in general can be any suitable diameter that allows the pig to maintain a seal in the pipe, so a fluid such as compressed air can propel the pig through the pipe.
• the diameter of the compressible sponge is about 1.4 times, about 2 times, or about 3.5 times the maximum inner diameter of the pipe to be treated. Those diameters refer to the sponge in an uncompressed state. In certain embodiments, the compressible sponge is spherical in an uncompressed state.
• Some other embodiments employ a cleaning composition that comprises one or more carboxylic acids.
• the cleaning composition comprises acetic acid, formic acid, propionic acid, 2-ethylhexanoic acid, or a combination of two or more thereof.
• the first cleaning composition consists essentially of 2- ethylhexanoic acid.
• the second cleaning composition can be the same or different from the first cleaning composition.
• Additional embodiments provide a method for forming at least one metal oxide on an interior surface of an industrial fluid processing or transport system or a component thereof, comprising: placing at least one first pig proximate to the interior surface of the industrial fluid processing or transport system or the component thereof; applying at least one cleaning composition to the interior surface with the at least one first pig; substantially removing the at least one cleaning composition from the interior surface; placing at least one second pig proximate to the interior surface of the industrial fluid processing or transport system or the component thereof; applying at least one metal compound to the interior surface with the at least one second pig; and converting at least some of the at least one metal compound to at least one metal oxide.
• Still other embodiments of the present invention employ at least two applications of the same or different metal compounds to the interior surface of an industrial fluid processing or transport system, such as a pipe, wherein two different temperatures are used.
• an industrial fluid processing or transport system such as a pipe
• certain embodiments provide a method for forming at least one metal oxide on an interior surface of an industrial fluid processing or transport system or a component thereof, comprising: placing at least one first pig proximate to the interior surface of the industrial fluid processing or transport system or the component thereof; applying at least one first metal compound to the interior surface with the at least one first pig; heating the environment of the interior surface to a temperature ranging from about
• Some embodiments of the present invention provide a method for decreasing or preventing fouling on a surface of a sensor, or a component thereof. Further embodiments provide a sensor comprising at least one surface comprising at least one metal oxide. In still further embodiments, the at least one surface of the sensor comprises at least one metal oxide, in which at least some of the at least one metal oxide is present in a diffused coating. Sensors may contain more than one part, including but not limited to the sensing element(s), mounting structures, and feedback means such as for example wiring which may be in protective cladding. Each of those parts have surfaces that may benefit from a metal oxide coating; one or more of those surfaces can be coated in accordance with the invention.
• Sensors that appear in embodiments of the present invention include, but are not limited to, sight glasses, for example a sight glass on a boiler, thermocouples, resistance thermal devices (RTDs), pressure sensors, flow rate and mass flow sensors, airspeed sensors, piezoelectric sensors, photo-optic combustion sensors, high temperature chromatographs, optical sensors, UV sensors, infra red sensors, electromagnetic field sensors, electromagnetic wave sensors, radiation sensors, toxic chemical sensors, gas analyzers, oxygen sensors, nitrogen sensors, NO x sensors, SO x sensors, CO 2 sensors, CO sensors, diesel exhaust soot sensors, other soot sensors, H 2 S sensors, and humidity sensors, among others.
• sight glasses for example a sight glass on a boiler, thermocouples, resistance thermal devices (RTDs), pressure sensors, flow rate and mass flow sensors, airspeed sensors, piezoelectric sensors, photo-optic combustion sensors, high temperature chromatographs, optical sensors, UV sensors, infra red sensors, electromagnetic field sensors, electromagnetic wave sensors, radiation sensors, toxic chemical sensors, gas analyzers,
• Some embodiments of the present invention provide a metal oxide coating on a surface that is subject to coke buildup.
• Such surfaces include, but are not limited to, one or more surfaces of: the heaters, heat exchangers, vacuum tower, and pipes that contact the heavier fractions in a crude unit or a vacuum unit; the furnace, heater tubes, furnace outlets, and pipes of an ethylene cracker unit; the heaters, heater tubes, fractionator bottoms, stripper bottoms, heat exchangers, and pipes of a delayed coker unit or a viscosity breaker; the cyclone dip legs and stripper baffles of the reactor, the reactor overhead line, the spent catalyst return line, the plenum of the catalyst regenerator, and the bottom and lower trays of the fractionator of a fluid catalytic cracking unit; the heaters, heater tubes, reactors, product pipes, catalyst transfer pipes, and valves of a continuous catalytic reforming unit; the heaters, heater tubes, reactors, and pipes in a fixed bed catalytic reforming unit; and the reactors, heaters, heat exchangers, and pipes of a syngas generation unit.
• Other embodiments provide a metal oxide coating on a surface that is subject to corrosive attack by one or more species present in the process stream.
• Such surfaces include, but are not limited to, one or more surfaces of: the furnaces, towers, strippers, reheaters, heat exchangers, and pipes of a crude unit or a vacuum unit; the fractionators, strippers, compressors, heat exchangers, and pipes of a delayed coker unit; a fractionator and pipes therefrom of a fluid catalytic cracking unit; on the knock-out drums, pipes, compressors, reheaters, and heat exchangers of a catalytic cracker's light ends recovery unit; the heat exchangers, product separators, debutanizer, overhead condensers, overhead drums, and pipes of a continuous catalytic reforming unit; the reactors, stabilizers, accumulators, heat exchangers, and pipes of a fixed bed catalytic reforming unit; the reactors, heaters, water washers, separators, hydrogen recycle compressors,
• combustion buildup can be any material that deposits on such surfaces, including, for example, slag, scale, coke, soot, and combinations thereof.
• a flame-heated surface includes any surface exposed to fuel combustion and its products, such as, for example, those surfaces exposed to the flame, smoke, soot, and/or fumes of combustion, even if that surface is not directly contacted by a flame.
• Such surfaces include, but are not limited to, insides of furnaces, preheaters, reheaters, and smoke stacks; outsides of boilers, heater tubes, and flame-heated reactors; as well as fuel conduits, valves, vents, burners, combustion control devices, ash conduits, and the like proximate to the combustion area.
• a flame-heated surface does not necessarily include process fluid-contacting surfaces. To illustrate, it is contemplated that heat is transferred from the flame-heated surface through the vessel wall to the process fluid-contacting surface.
• a vessel wall has in general two surfaces, the flame-heated surface and the process fluid-contacting surface.
• Combustion engine systems include, but are not limited to, internal combustion engines, two-stroke engines, four-stroke engines, gasoline engines, diesel engines, turboprop engines, jet engines, gas turbines, and rocket engines.
• Suitable metal surfaces include, but are not limited to, jet, turbojet, turbofan, ram jet, scram jet, and turbine engine surfaces including inlet, compressor, turbine, blades, recuperators, afterburner, nozzle, thrust vector surfaces, and fuel delivery components; internal combustion engine surfaces including pistons, rotors, cylinders, housings, piston rings, seals, endplates, cylinder heads, valve heads, valve stems, valve seats, valve faces, valve train components, cams, pushrods, cam followers, rocker arms, valve springs, valve guides, combustion chambers, crankcases, intake system components, supercharger components, exhaust manifolds, exhaust gas recirculation pipes and valves, turbocharger components, catalytic converter components, exhaust pipes, fuel injectors, and fuel pumps; and rocket engine surfaces including inlets, fuel delivery systems, fuel combustion zones, and thrust vector surfaces.
• the metal oxide coating of the metal surface of a combustion engine system is an oxidizing coating.
• the metal oxide coating further comprises at least one metal.
• Metals that may be desired, such as for catalytic purposes, for example, include but are not limited to platinum, palladium, rhodium, nickel, cerium, gold, silver, zinc, lead, rhenium, ruthenium, and combinations of two or more thereof.
• Still other embodiments provide a fluid processing or transport system comprising at least one surface comprising at least one metal oxide coating, in which the system has a large size. A large size is useful for commercial scale processes.
• Industrial fluid processing or transport systems include, but are not limited to, oil refineries; oil refinery subsystems such as crude units, atmospheric units, vacuum units, delayed cokers, fluid catalytic crackers, fixed bed catalytic crackers, continuous catalytic reformers, naphtha reformers, hydrotreaters, hydrocrackers, alkylators including sulfuric acid alkylators and HF alkylators, amine treaters, sulfur recovery units, sour water strippers, isomerization units, and hydrogen reforming units; waste water treatment plants; cooling water systems such as those found in manufacturing plants and power plants; desalinization plants; and processing systems found in colorants manufacturing, cosmetics manufacturing, food processing, chemical manufacturing, pharmaceutical manufacturing, and the like.
• oil refinery subsystems such as crude units, atmospheric units, vacuum units, delayed cokers, fluid catalytic crackers, fixed bed catalytic crackers, continuous catalytic reformers, naphtha reformers, hydrotreaters, hydrocrackers, alkylators including sulfuric acid alkylators and HF
• the surface of the fluid processing or transport system to receive a metal oxide coating in accordance with the present invention has a surface area greater than about 100 square feet.
• the surface area ranges between about 100 square feet to about 500 square feet, between about 500 square feet to about 1,000 square feet, between about 1 ,000 square feet to about 10,000 square feet, between about 10,000 square feet to about 20,000 square feet, between about 20,000 square feet to about 50,000 square feet, between about 50,000 square feet to about 100,000 square feet, between about 100,000 square feet to about 1 ,000,000 square feet, between about 1 ,000,000 square feet to about 10,000,000 square feet, between about 10,000,000 square feet to about 1 square mile, between about 1 square mile to about 5 square miles, between about 5 square miles to about 10 square miles, or greater than about 10 square miles.
• the surface to be treated according to the invention also can be pretreated, in further embodiments, before the application of the composition.
• the surface can be etched according to known methods, for example, with an acid wash comprising nitric acid, sulphuric acid, hydrochloric acid, phosphoric acid, carboxylic acid, or a combination of two or more thereof, or with a base wash comprising sodium hydroxide or potassium hydroxide, for example.
• the surface can be mechanically machined or polished, with or without the aid of one or more chemical etching agents, abrasives, and polishing agents, to make the surface either rougher or smoother.
• the surface can be pretreated such as by carburizing, nitriding, painting, powder coating, plating, or anodizing.
• Thin films of chrome, tin, and other elements, alone or in combination, can be deposited, in some embodiments. Methods for depositing thin films are well known and include chemical vapor deposition, physical vapor deposition, molecular beam epitaxy, plasma spraying, electroplating, ion impregnation, and others.
• a metal compound comprises a transition metal atom.
• a metal compound comprises a rare earth metal atom.
• the metal compound composition comprises a plurality of metal compounds.
• a plurality of metal compounds comprises at least one rare earth metal compound and at least one transition metal compound, while in other embodiments, a plurality of metal compounds comprises other than at least one rare earth metal compound and at least one transition metal compound.
• Metal carboxylates, metal alkoxides, and metal ⁇ -diketonates can be chosen for some embodiments of the present invention.
• a metal compound mixture comprises one metal compound as its major component and one or more additional metal compounds which may function as stabilizing additives.
• Stabilizing additives in some embodiments, comprise trivalent metal compounds. Trivalent metal compounds include, but are not limited to, chromium, iron, manganese, and nickel compounds.
• a metal compound composition in some embodiments, comprises both cerium and chromium compounds.
• the metal compound that is the major component of the metal compound composition contains an amount of metal that ranges from about 65 to about 97% by weight or from about 80 to about 87% by weight of the total weight of metal in the composition.
• the amount of metal forming the major component of the metal compound composition ranges from about 90 to about 97% by weight of the total metal present in the composition. In still other embodiments, the amount of metal forming the major component of the metal compound composition ranges from about 97 to about 100% by weight of the total metal present in the composition.
• the metal compounds that may function as stabilizing additives may be present in amounts such that the total amount of the metal in metal compounds which are the stabilizing additives is at least 3% by weight, relative to the total weight of the metal in the metal compound composition. This can be achieved in some embodiments by using a single stabilizing additive, or multiple stabilizing additives, provided that the total weight of the metal in the stabilizing additives is greater than 3%. In other embodiments, the amount of the stabilizing metal is less than 3 % relative to the total weight of metal in the metal compound composition. In yet other embodiments, the total weight of the metal in the stabilizing additives ranges from about 3% to about 35% by weight.
• the total weight for the metal in the stabilizing additives ranges from about 3 to about 30% by weight, relative to the total weight of the metal in the metal compound composition. In other embodiments, the total weight range for the metal in the stabilizing additives ranges from about 3 to about 10% by weight. In some embodiments, the total weight range for the metal in the stabilizing additives is from about 7 to about 8% by weight, relative to the total weight of the metal in the metal compound composition. Still other embodiments provide the stabilizing metal in an amount greater than about 35 % by weight relative to the total weight of the metal in the metal compound composition. [00186] The amount of metal in the metal compound composition, according to some embodiments, ranges from about 20 to about 150 grams of metal per kilogram of metal compound composition.
• the amount of metal in the metal compound composition ranges from about 30 to about 50 grams of metal per kilogram of metal compound composition. In further embodiments, the metal compound composition can contain from about 30 to about 40 grams of metal per kg of composition. Amounts of metal less than 20 grams of metal per kilogram of metal compound composition or greater than about 150 grams of metal per kilogram of metal compound composition also can be used. [00187]
• the metal compound may be present in any suitable composition. Finely divided powder, nanoparticles, solution, suspension, multi-phase composition, gel, vapor, aerosol, and paste, among others, are possible.
• the metal compound composition may also include nanoparticles in the size range of less than 100 nm in average size and being composed of a variety of elements or combination thereof, for example, Al 2 O 3 , CeO 2 , Ce 2 O 3 , TiO 2 , ZrO 2 and others.
• the nanoparticles can be dispersed, agglomerated, or a mixture of dispersed and agglomerated nanoparticles. Nanoparticles may have a charge applied to them, negative or positive, to aid dispersion.
• dispersion agents such as known acids or surface modifying agents, may be used.
• nanoparticles may decrease the porosity of the final coating; the level of porosity will generally decrease with increasing quantity and decreasing size of the included nanoparticles.
• Coating porosity can also be influenced by applying additional coating layers according to the process of the invention; porosity will generally decrease with an increasing number of layers.
• the nanoparticles may be first mixed with a liquid and then mixed with the compound composition; this method provides a means to create a fine dispersion in a first liquid which retains its dispersion when mixed with a second, or third liquid.
• nanoparticles of chosen elements, oxides, molecules, or alloys may be dispersed into a first liquid and, after a desired quality of dispersion is achieved, the nanoparticles in the first liquid may be mixed with the liquid metal compound composition prior to the exposure of the final composition to an environment that will convert at least a portion of the metal compound(s) into metal oxides.
• the result may be a more dense film with reduced porous sites.
• the applying of the metal compound composition may be accomplished by various processes, including dipping, spraying, flushing, vapor deposition, printing, lithography, rolling, spin coating, brushing, swabbing (e.g., with an absorbent "pig" of fabric or other material that contains the metal compound composition and is drawn through the apparatus), pig train (in which the metal compound composition, trapped between two or more pigs, is pushed through a system by compressed air, for example), or any other means that allows the metal compound composition to contact the desired portions of the surface to be treated.
• the metal compound composition may be liquid, and may also comprise a solvent.
• the optional solvent may be any hydrocarbon and mixtures thereof.
• the solvent can be chosen from carboxylic acids; toluene; xylene; benzene; alkanes, such as for example, propane, butane, isobutene, hexane, heptane, octane, and decane; alcohols, such as methanol, ethanol, n-propanol, isopropanol, n-butanol, and isobutanol; mineral spirits; ⁇ -diketones, such as acetylacetone; ketones such as acetone; high- paraffin, aromatic hydrocarbons; and combinations of two or more of the foregoing.
• carboxylic acids such as for example, propane, butane, isobutene, hexane, heptane, octane, and decane
• alcohols such as methanol, ethanol, n-propanol, isopropanol, n-butanol, and isobutano
• the metal compound composition further comprises at least one carboxylic acid. Some embodiments employ no solvent in the metal compound composition. Other embodiments employ no carboxylic acid in the metal compound composition.
• the metal compound composition can applied in some embodiments in which the composition has a temperature less than about 250 0 C. That composition also can be applied to the substrate in further embodiments at a temperature less than about 50 0 C. In other embodiments, the liquid metal compound composition is applied to the substrate at room temperature. In still other embodiments, that composition is applied at a temperature greater than about 250 0 C. [00191] Following application, the at least one metal compound is at least partially converted to at least one metal oxide. In some embodiments the at least one metal compound is fully converted to at least one metal oxide.
• Suitable environments for converting the at least one metal compound into at least one metal oxide include vacuum, partial vacuum, atmospheric pressure, high pressure equal to several atmospheres, high pressure equal to several hundred atmospheres, inert gases, and reactive gases such as gases comprising oxygen, including pure oxygen, air, dry air, and mixtures of oxygen in various ratios with one or more other gases such as nitrogen, carbon dioxide, helium, neon, and argon, as well as hydrogen, mixtures of hydrogen in various ratios with one or more other gases such as nitrogen, carbon dioxide, helium, neon, and argon, also other gases such as, for example, nitrogen, NH 3 , hydrocarbons, H 2 S, PH 3 , each alone or in combination with various gases, and still other gases which may or may not be inert in the converting environment.
• a suitable environment for converting the at least one metal compound into at least one metal oxide is free or substantially free of oxygen.
• the environment may be heated relative to ambient conditions, in some embodiments.
• the environment may comprise reactive species that cause or catalyze the conversion of the metal compound to the metal oxide, such as, for example, acid-catalyzed hydrolysis of metal alkoxides.
• the metal compound is caused to convert to the metal oxide by the use of induction heating, lasers, microwave emission, or plasma, as explained below.
• the conversion environment may be accomplished in a number of ways. For example, a conventional oven may be used to bring the coated substrate up to a temperature exceeding approximately 25O 0 C for a given period of time. In some embodiments, the environment of the coated substrate is heated to a temperature exceeding about 400 0 C but less than about 45O 0 C or less than about 500 0 C for a chosen period of time. In other embodiments, the environment of the coated substrate is heated to a temperature ranging from about 400 0 C to about 65O 0 C. In further embodiments, the environment is heated to a temperature ranging from about 400 0 C to about 55O 0 C.
• the environment is heated to a temperature ranging from about 550 0 C to about 650 0 C, from about 650 0 C to about 800 0 C, or from about 800 0 C to about 1000 0 C. In one embodiment, the environment is heated to a temperature of up to about 425 0 C or 45O 0 C. Depending on the size of the components and/or process equipment, pipes, etc., the time period may be extended such that sufficient conversion of a desired amount of the metal compound to metal oxides has been accomplished.
• the oxidation of the surface being treated is not desired.
• an inert atmosphere may be provided in the conversion environment to prevent such oxidation.
• a nitrogen or argon atmosphere can be used, among other inert gases, to prevent or reduce the oxidation of the surface prior to or during the conversion process.
• the conversion environment may also be created using induction heating through means familiar to those skilled in the art of induction heating.
• the conversion environment may be provided using a laser applied to the surface area for sufficient time to allow at least some of the metal compounds to convert to metal oxides.
• the conversion environment may be created using an infra-red light source which can reach sufficient temperatures to convert at least some of the metal compounds to metal oxides.
• Some embodiments may employ a microwave emission device to cause at least some of the metal compound to convert.
• Still other embodiments employ a plasma to provide the environment for converting the metal compound into metal oxide.
• the conversion environment can be created without the use of an inert gaseous environment, thus enabling conversion to be done in open air, outside of a closed system due to the reduced time for undesirable compounds to develop on the material's surface in the presence of ambient air.
• the gas above the metal compound on the surface can be heated, in some embodiments, to convert the metal compound to the metal oxide.
• Heating can be accomplished by introducing high temperature process gases, which are fed through the assembled fluid transport or processing system, wherein the joints, welds, connections, and one or more interior surfaces of the fluid transport or processing system become covered with a protective thin film of the desired metal oxide(s).
• This high temperature gas can be produced by a conventional oven, induction heating coils, heat exchangers, industrial process furnaces, exothermic reactions, microwave emission, or other suitable heating method.
• these can be temporarily bypassed using known methods of piping, valves, ports, etc.
• the metal compound composition may be applied to chosen areas of a component or system and an induction heating element may be passed proximate to the area of interest to create the conversion environment.
• the inner surface of a component may not be visible by line of sight, but an induction wand held proximate to the inside or outside surfaces of the component may allow sufficient heat to be developed on the wetted surfaces being treated with the metal compounds such that the desired oxides are formed by an indirect heating method.
• This technique would also be possible using infra-red heating from inside or outside of a component, flame heating, or other known heating methods wherein the material of the component can be raised to the desired temperature to ensure the conversion of the metal compounds to oxides.
• this method of indirect heating may also be used with a chosen atmosphere that may be provided proximate to the wetted surfaces of the pipe or component, such as an inert atmosphere made up of argon, as one example, which would serve to prevent undesirable oxides to form on the material surface being treated.
• a chosen atmosphere that may be provided proximate to the wetted surfaces of the pipe or component, such as an inert atmosphere made up of argon, as one example, which would serve to prevent undesirable oxides to form on the material surface being treated.
• multiple coats may be desired such that further protection of the material's surface is provided.
• cooling methods may be used after each heating cycle to bring the surfaces to the required temperatures prior to subsequent applications of the metal compounds. Such cooling methods may be used that are known to the art such as water spraying, cold vapor purging through the interior of the system, evaporative cooling methods, and others.
• compositions that have been found to be suitable in embodiments of the present invention include, but are not limited to:
• ZrO 2 for example, at 0-90 wt% CeO 2 for example, at 0-90 wt%
• CeO 2 -ZrO 2 where CeO 2 is about 10-90 wt%
• TiO 2 for example, at 0-90 wt%
• NiO for example, at 0-90 wt%
• Al 2 O 3 for example, at 0-90 wt%
• Oxides of the following elements also can be used in embodiments of the present invention: Lithium, Beryllium, Sodium, Magnesium, Aluminum, Silicon, Potassium, Calcium, Scandium, Titanium, Vanadium, Chromium, Manganese, Iron, Cobalt, Nickel, Copper, Zinc, Gallium, Germanium, Arsenic, Bromine, Rubidium, Strontium, Yttrium, Zirconium, Niobium, Molybdenum, Technetium, Ruthenium, Rhodium, Palladium, Antimony, Tellurium, Silver, Cadmium, Indium, Tin, Cesium, Barium, Lanthanum, Cerium, Praseodymium, Neodymium, Promethium, Samarium, Europium, Gadolinium, Terbium, Dysprosium, Holmium, Erbium, Thulium, Ytterbium, Lutetium, Hafnium,
• SrTiO 3 and MgAl 2 O 4 are included. Those materials are likely to form at least in small amounts when appropriate metal compounds are used, depending on the conditions of the conversion process.
• the molar ratio of metal compounds deposited on the surface corresponds to the molar ratio of metal oxides after conversion.
• the invention relates, in some embodiments, to diffused coatings and thin films (and articles coated therewith) containing at least one rare earth metal oxide, and at least one transition metal oxide.
• diffusion of metal oxides can range in concentration from rare interstitial inclusions in the substrate, up to the formation of materials that contain significant amounts of metal oxide.
• a thin film is understood to indicate a layer, no matter how thin, composed substantially of metal oxide. In some embodiments, a thin film has very little or no substrate material present, while in other embodiments, a thin film comprises atoms, molecules, nanoparticles, or larger domains of substrate ingredients. In some embodiments, it may be possible to distinguish between diffused portions and thin films.
• a gradient may exist in which it becomes difficult to observe a boundary between the diffused coating and the thin film.
• some embodiments may exhibit only one of a diffused coating and a thin film.
• Still other embodiments include thin films in which one or more species have migrated from the substrate into the thin film.
• the terms "metal oxide coating” and "surface comprises at least one metal oxide” include all of those possibilities, including diffused coatings, thin films, stacked thin films, and combinations thereof.
• the diffused coating penetrates the substrate to a depth of less than about 100 Angstroms. In other embodiments, the diffused coating penetrates from about 100 Angstroms to about 200 Angstroms, from about 200 Angstroms to about 400 Angstroms, from about 400 Angstroms to about 600 Angstroms, and greater than about 600 Angstroms, and in some embodiments from about 200 to about 600 Angstroms.
• This diffused coating allows much thinner films [in some embodiments around 0.1 to 1 microns in thickness (or about 0.5 microns when approximately 6 layers are used)] to be applied, and yet may provide equivalent protection to that provided by conventional coating or thin film technologies. This, in turn, allows for thinner films or coatings to be established, reducing significantly the cost of materials attaching to the substrate.
• some embodiments of the present invention provide a thin film no thicker than about 5 nm.
• Other embodiments provide a thin film no thicker than about 10 nm.
• Still other embodiments provide a thin film no thicker than about 20 nm.
• Still other embodiments provide a thin film no thicker than about 100 nm.
• Other embodiments provide a thin film having a thickness less than about 25 microns.
• Still other embodiments provide a thin film having a thickness less than about 20 microns.
• Still other embodiments provide a thin film having a thickness less than about 10 microns.
• Yet other embodiments provide a thin film having a thickness less than about 5 microns.
• Some embodiments provide a thin film having a thickness less than about 2.5 microns.
• Even other embodiments provide a thin film having a thickness less than about 1 micron.
• the metal oxide coating can contain other species, such as, for example, species that have migrated from the substrate into the metal oxide coating.
• those other species can come from the atmosphere in which the at least one metal compound is converted.
• the conversion can be performed in an environment in which other species are provided via known vapor deposition methods.
• Still other embodiments provide other species present in or derived from the at least one metal compound or the composition comprising the compound. Suitable other species include metal atoms, metal compounds including those metal atoms, such as oxides, carbides, nitrides, sulfides, phosphides, and mixtures thereof, and the like.
• the inclusion of other species can be accomplished by controlling the conditions during conversion, such as the use of a chosen atmosphere during the heat conversion process, for example, a partial vacuum or atmosphere containing O 2 , N 2 , NH 3 , one or more hydrocarbons, H 2 S, alkylthiols, PH 3 , or a combination thereof.
• a chosen atmosphere during the heat conversion process for example, a partial vacuum or atmosphere containing O 2 , N 2 , NH 3 , one or more hydrocarbons, H 2 S, alkylthiols, PH 3 , or a combination thereof.
• Some embodiments of the present invention provide metal oxide coatings that are substantially free of other species.
• small amounts of carbides may form along side oxides when, for example, metal carboxylates are converted, if no special measures are taken to eliminate the carbon from the carboxylate ligands.
• converting metal compounds in the presence of oxygen gas, air, or oxygen mixed with other gases reduces or eliminates carbide formation in some embodiments of the present invention.
• rapid heating of the conversion environment such as, for example, by induction heating, microwave heating, lasers, plasmas, and other heating methods that can produce the necessary heat levels in a short time, reduces or eliminates formation of other species, in other embodiments. At least one rapid heating technique is used in combination with an oxygen-containing atmosphere in still other embodiments.
• Additional embodiments employ various heating steps to reduce or eliminate the formation of other species.
• carbide formation can be lessened during metal oxide formation in some embodiments by applying a metal compound precursor composition containing a metal carboxylate to a surface, subjecting the surface to a low-temperature bake at about 250 0 C under a vacuum, introducing air and maintaining the temperature, and then increasing the temperature to about 420 0 C under vacuum or inert atmosphere to convert the metal carboxylate into the metal oxide.
• a low-temperature bake drives off most or all of the carboxylate ligand, resulting in an oxide film substantially free of metal carbide.
• a base coat of at least one metal oxide is formed from at least one metal carboxylate under an inert atmosphere.
• a base coat may contain metal carbides due to the initial presence of the carboxylate ligands.
• a base coat may exhibit good adhesion and strength, for example, when the surface comprises a carbon steel alloy.
• one or more subsequent metal compounds are repeatedly applied and converted in an oxygen-containing atmosphere, for example, and the subsequent layers of metal oxide form substantially without metal carbides.
• six or more layers are formed on the base coat.
• the effect of any mismatches in physical, chemical, or crystallographic properties may be minimized by the use of much thinner coating materials and the resulting films.
• the smaller crystallite structure of the film (3-6 nanometers, in some embodiments) increases Hall-Petch strength in the film's structure significantly.
• the present invention provides methods of reducing differences in coefficients of thermal expansion between a substrate and a metal oxide coating proximal to the substrate.
• methods of reducing differences in coefficients of thermal expansion between a substrate and at least one metal oxide comprise interposing a diffused coating between the substrate and the metal oxide. Interposing such a diffused coating comprises applying at least one metal compound to the substrate, and then at least partially converting the at least one metal compound to at least one metal oxide.
• the thermal stability of the metal oxide coating can be tested, in some embodiments, by exposing the coated material to thermal shock. For example, a surface having a metal oxide coating can be observed, such as by microscopy.
• the surface can be exposed to a thermal shock, such as by rapid heating or by rapid cooling.
• Rapid cooling can be caused by, for example, dunking the room-temperature or hotter surface into liquid nitrogen, maintaining the surface under liquid nitrogen for a time, and then removing the surface from the liquid nitrogen.
• the surface is then observed again, to look for signs that the metal oxide coating is delaminating, cracking, or otherwise degrading because of the thermal shock.
• the thermal shock test can be repeated to see how many shock cycles a given metal oxide coating can withstand before a given degree of degradation, if any, is observed.
• the at least one metal oxide coating withstands at least one, at least five, at least ten, at least twenty-five, at least fifty, or at least one hundred thermal shock cycles from room temperature to liquid nitrogen temperature.
• the nanocrystalline grains resulting from some embodiments of the methods of the present invention have an average size, or diameter, of less than about 50 nm.
• nanocrystalline grains of metal oxide have an average size ranging from about 1 nm to about 40 nm or from about 5 nm to about 30 nm.
• nanocrystalline grains have an average size ranging from about 10 nm to about 25 nm.
• nanocrystalline grains have an average size of less than about 10 nm, or less than about 5 nm.
• the invention relates to metal oxide coatings (whether diffused, thin film, or both diffused and thin film) and articles comprising such coatings, in which the coatings contain two or more rare earth metal oxides and at least one transition metal oxide. Further embodiments of the invention relate to metal oxide coatings (and articles comprising them), containing ceria, a second rare earth metal oxide, and a transition metal oxide. Some embodiments relate to metal oxide coatings (and articles comprising them), containing yttria, zirconia, and a second rare earth metal oxide.
• the second rare earth metal oxide can include platinum or other known catalytic elements.
• the metal compound applied to the surface comprises a cerium compound, and the metal oxide coating comprises cerium oxide (or ceria).
• the metal compound applied to the surface comprises a zirconium compound, and the metal oxide coating comprises zirconia.
• a solution comprising both a cerium compound and a zirconium compound is applied, and the resulting metal oxide coating comprises ceria and zirconia.
• the zirconia formed by the process of the invention comprises crystal grains having an average size of about 3-9 nm
• the ceria formed by the process of the invention comprises crystal grains having an average size of about 9-18 nm.
• the nanostructured zirconia can be stabilized in some embodiments with yttria or other stabilizing species alone or in combination.
• the metal oxide coating comprises zirconia, yttria, or alumina, each alone or in combination with one or both of the others.
• the method of the invention further includes a step of applying an organosiloxane-silica composition over the formed oxide coating and exposing the coated substrate to an environment that will remove volatile components from the composition without decomposing organo-silicon bonds.
• other treatments can be performed after the formation of an oxide coating.
• additional metal oxide coatings which can be the same or different, can be added.
• the metal oxide(s) can be etched, polished, carburized, nitrided, painted, powder coated, plated, or anodized.
• the at least one metal oxide serves as a bond coat for at least one additional coating. Such additional coatings need not be formed according to the present invention.
• Some embodiments provide a metal oxide bond coat that allows an additional coating that would not adhere to the surface as well in the absence of the bond coat.
• the substrate can be subjected to a thermal treatment, either before or after a metal oxide coating is formed on the substrate.
• a substrate having a metal oxide coating in accordance with the present invention can be annealed at high temperature to strengthen the substrate.
• a substrate can be held near absolute zero before or after a metal oxide coating is formed on the substrate.
• Suitable temperatures for thermal treatment range from nearly 0 K to several thousand K, and include liquid hydrogen, liquid helium, liquid neon, liquid argon, liquid krypton, liquid xenon, liquid radon, liquid nitrogen, liquid oxygen, liquid air, and solid carbon dioxide temperatures, and temperatures obtained by mixtures, azeotropes, and vapors of those and other materials.
• the methods of the present invention can be used during or after manufacturing a given component of a fluid processing or transport system.
• one or more oxide coatings can be applied to a pipe section as it is manufactured, or after the pipe is assembled into a fluid processing or transport system.
• the methods of the present invention can be incorporated into conventional manufacturing steps. For example, after pipes are welded, often they are subjected to a heat treatment to relieve the stresses introduced by the welding process.
• at least one metal compound is applied after welding and before that heat treatment. In those embodiments, that one heat treatment converts at least one metal compound into at least one metal oxide and relieves welding-induced stresses.
• the process of the invention may permit the use of coatings on a wide variety of materials, including application of CeO 2 and ZrO 2 coatings to ceramics and/or solid metals previously not thought possible of being coated with these materials.
• Some embodiments of the present invention provide a relatively low temperature process that does not damage or distort many substrates, does not produce toxic or corrosive water materials, and can be done on site, or "in the field" without the procurement of expensive capital equipment.
• the nature of the resulting interstitial boundaries of the invention's nanocrystalline structures in various embodiments can be comprised of chosen ingredients so as to increase ionic conductivity while decreasing electron conductivity, or can be comprised of chosen ingredients so as to increase the material's mixed conductivity, or to modify its porosity. In a similar fashion, many other properties may be altered through the judicious selection of various ingredients that are formulated as part of the metal compound composition of the invention.
• a substrate which comprises at least a portion of a component's structure is placed within a vacuum chamber, and the chamber is evacuated.
• the substrate can be heated or cooled, for example, with gas introduced into the chamber or by heat transfer fluid flowing through the substrate mounting structure. If a gas is introduced, care should be taken that it will not alter the substrate in an unintended manner, such as by oxidation of a hot iron-containing surface by an oxygen-containing gas. Introduced gas optionally can be evacuated once the substrate achieves the desired temperature. Vapor of one or more metal compounds, such as cerium(III) 2-hexanoate, enters the vacuum chamber and deposits on the substrate. A specific volume of a fluid composition containing the metal compound can provide a specific amount of compound to the surface of the substrate within the vacuum chamber, depending on the size of the chamber and other factors.
• a chosen gas is vented into the chamber and fills the vacuum chamber to a chosen pressure, in one example, equal to one atmosphere.
• the chamber is heated to a temperature sufficient to convert at least some of the compounds into oxides, for example, 450 °C, for a discrete amount of time sufficient for the conversion process, for example, thirty minutes.
• a ceria layer forms on the substrate.
• the process can be repeated as many times as desired, forming a thicker coating of ceria on the substrate.
• the component can be cooled relative to ambient temperature, such as, for example, to liquid nitrogen temperature, to aid the deposition process.
• a reducing atmosphere may be used to convert at least a portion of the metal oxides to metal.
• the substrate can comprise one or more polymers, such as polyvinyl chloride.
• the polymer substrate can be kept at lower temperatures sufficient to prevent the degradation of the substrate during the heating process, for example, at liquid nitrogen temperatures while the metal compound converts to the oxide due to any technique that heats the metal compound but not the substrate to a significant degree. Examples of such heating techniques include flash lamps, lasers, and microwave heating.
• materials that would become degraded by exposure to high temperatures can be kept at lower temperatures using the same techniques. For example, glasses, low-melting-temperature metals, polycarbonates, and similar substrates can be kept cooler while the at least one metal compound is converted to at least one metal oxide.
• the term "high temperature” means a temperature sufficiently high to convert the metal compound to metal oxide, generally in the range of about 200 0 C to about 1000 °C, such as, for example, about 200 0 C to about 400 0 C, or about 400 0 C to about 500 0 C, about 500 0 C to about 650 0 C, about 650 0 C to about 800 0 C, or about 800 0 C to about 1000 0 C.
• Process gases at even higher temperatures can be used, so that, when the gas is passed through the fluid transport or processing system during the process of some embodiments of the invention, the temperature of the gas exiting the system is within the range given above.
• a given embodiment of the invention described herein may involve one or more of several basic concepts.
• one concept relates to a surface treatment that generally meets above-described technical properties and can be manufactured at a low cost.
• Another concept relates to a method to form an oxide protective film on the surface of a metal.
• Another concept relates to a two-step process adapted to form a prophylactic layer onto internal surfaces of a fluid transport or processing system.
• Another concept relates to creating thin films of nanocrystalline zirconia on surfaces to resist fibrous growth of carbon and other elements.
• Another concept is related to a means to apply a protective coating to an assembly of various components using a process to heat an enclosed system as a curing method for the coating.
• an oxidizing coating may be formed on a substrate by applying a liquid metal compound composition to the substrate using a dipping process, spraying, vapor deposition, swabbing, brushing, or other known means of applying a liquid to an internal surface of a pipe, conduit or process equipment.
• This liquid metal compound composition comprises at least one rare earth metal salt of a carboxylic acid and at least one transition metal salt of a carboxylic acid, in a solvent, in some embodiments.
• the surface, once wetted with the composition is then exposed to a heated environment that will convert at least some of the metal compounds to metal oxides, thereby forming an oxidizing coating on the substrate.
• the metal oxide coatings resulting from the conversion process are applied to material substrates to form one or more thin protective layers. Additional applications of the metal compounds followed by conversion environment exposure (e.g., heating the surface through means described above) may be done to create multiple layers of thin film oxides stacked one on another.
• the process may be used to create a nanocrystalline structure that comprises an oxygen containing molecule for chosen applications.
• the resulting nanocrystalline structure may comprise a metal containing compound, a metal, a ceramic, or a cermet.
• One benefit to some embodiments of the invention is the ability to apply the metal compound composition to an assembled system and then to flush high temperature gases through the system to achieve the conversion process, resulting in a well-dispersed metal oxide coating on all interior surfaces. This is especially beneficial for welded piping systems, heat exchangers, and similar components which use welding for their assembly, said welding typically destroying whatever surface treatments were applied to the pipes, heat exchangers, or other parts prior to welding. The high temperature conditions of the welding process tend to destroy all protective coatings.
• the invention provides a way to create a final metal oxide coating covering all parts of the process system, creating a protective coating for weld joints and component interiors alike.
• material may be added to the base fluid to act as filler material.
• the porosity of the finished coating is altered through the inclusion of nanoparticles of chosen elements in the liquid metal compound composition prior to the exposure of the composition to an environment that will convert at least a portion of the metal compound(s) into metal oxides. The result is a more dense thin film.
• the treated substrate may be exposed to a reducing agent, such as hydrogen or other known reducing agent using known means for oxide reduction.
• a reducing agent such as hydrogen or other known reducing agent using known means for oxide reduction.
• 7 % hydrogen in argon heated to 350 0 C can be used to form platinum in certain embodiments.
• Other metals that may be desired, such as for catalytic purposes, for example, include but are not limited to platinum, palladium, rhodium, nickel, cerium, gold, silver, zinc, lead, rhenium, ruthenium, and combinations of two or more thereof.
• the method of the invention may be used to provide prophylactic coatings to internal surfaces of fluid transport or processing systems, and has particular utility in the area of fluid transport or processing systems in the petroleum and natural gas industries, where carbon fouling, corrosion, and hydrogen embrittlement are particular problems in pipelines and processing equipment.
• coating with the ceria, or yttria-stabilized zirconia, or a combination of ceria and zirconia will significantly reduce carbon fouling on steel surfaces exposed to petroleum or other hydrocarbons at temperatures of around 570 0 C, in effect providing protection against any effective or measurable carbon deposition.
• Uncoated steel surfaces exposed to similar conditions become sufficiently fouled with carbon as to require cleaning after about 18 months of service. Inhibition of carbon fouling occurs during exposure to petroleum or other hydrocarbons at temperatures as high as 900 0 C. Similar improvement in fouling will occur in fluid processing systems used to process natural gas.
• the method of the invention provides protection against other fouling and corrosion problems often encountered in chemical or hydrocarbon processing operations in various embodiments.
• the method of the invention provides a partial or full barrier against the intrusion of hydrogen into a metal substrate, reducing surface and substrate degradation through this known mechanism, in some embodiments.
• the method of the invention provides an effective barrier against corrosive attack in further embodiments. Because the resulting surface coating provides an effective barrier between the material of the process equipment (typically metal, such as iron or steel) and the environment (e.g., a crude oil, cracked hydrocarbon, or natural gas stream), electrochemical and other reactions between the metal and the process stream are effectively reduced or prevented in still other embodiments.
• the material of the process equipment typically metal, such as iron or steel
• the environment e.g., a crude oil, cracked hydrocarbon, or natural gas stream
• Heat exchangers pass thermal energy, whether for heating or cooling purposes, for example, between gases, between a gas and a liquid, between liquids, between a liquid and a solid, and between a gas and a solid.
• Heat exchangers for two-phased, semi-solid, paste and slurry systems are also known.
• Heat exchangers include, for example, oil refinery heating units, cooling towers, automobile radiators, HVAC systems such as air conditioners, solar towers, geothermal harvesters, refrigeration units, and the like.
• the materials that can be protected from fouling according to the present invention include any material that can receive a protective coating of a metal oxide.
• Such materials include, for example, metals, ceramics, glasses, and cermets, as well as composites and polymers that can withstand the process conditions for converting the metal carboxylate into metal oxide.
• the metals that can be protected include, but are not limited to, substantially pure metals, alloys, and steels, such as, for example, low alloy steels, carbon steels, stainless steels, 300 series stainless steel, 400 series stainless steel, nickel base alloys, high-chromium steels, and high-molybdenum steels.
• the industrial and commercial products that can be protected according to the present invention are not limited.
• Petroleum refinery petrochemical processing
• petroleum transport and storage such as pipelines, oil tankers, fuel transport vehicles, and gas station fuel tanks and pumps; sensors; industrial chemical manufacture, storage, and transportation; automotive fluid systems including fuel systems, lubrication systems, radiators, air heaters and coolers, break systems, power steering, transmissions, and similar hydraulics systems; aeronautical and aerospace fluid storage and transport systems including fuel systems and hydraulic systems; and food and dairy processing systems; combustion engines, turbine engines, and rocket engines; among many others, can benefit from the present invention.
• Zirconium 2-ethylhexanoate 28 % wt. of the final composition, Alfa-Aesar
• silicon 2-ethylhexanoate (33.5 % wt., Alfa-Aesar)
• chromium 2-ethylhexanoate (1 % wt., Alfa- Aesar) were mixed into 2-ethylhexanoic acid (37.5 % wt., Alfa-Aesar), and the composition was spin-coated onto the steel substrate.
• Silicon 2-ethylhexanoate (74 % wt., Alfa-Aesar), sodium 2-ethylhexanoate (5.2 % wt., Alfa-Aesar), calcium 2-ethylhexanoate (11 % wt., Alfa-Aesar), and chromium 2- ethylhexanoate (1.4 % wt., Alfa-Aesar) were mixed into 2-ethylhexanoic acid (8.4 % wt., Alfa-Aesar), and the composition was spin-coated onto the steel substrate.
• 2-ethylhexanoic acid 8.4 % wt., Alfa-Aesar
• YSZ Yttrium 2-ethylhexanoate powder (2.4 % wt., Alfa-Aesar) was dissolved into 2- ethylhexanoic acid (60 % wt., Alfa-Aesar) with stirring at 75-80 °C for one hour. Once the composition was cooled to room temperature, zirconium 2-ethylhexanoate (36.6 % wt., Alfa- Aesar) and chromium 2-ethylhexanoate (1 % wt., Alfa-Aesar) were mixed in. The composition was spin-coated onto the steel substrate.
• the coated steel coupons were placed in a vacuum oven, and evacuated to about 20-60 millitorr. The coupons were heated to 450 °C, and then allowed to cool to room temperature. The process of depositing and heating was repeated to apply eight coatings of the appropriate composition on each coupon.
• Each coated coupon was assembled into a test cell having a glass cylinder (I" inner diameter x 1.125" tall) clamped to the coated portion of the coupon.
• a rubber gasket formed a seal between the glass cylinder and the coupon.
• Aqua Regia was prepared from HNO 3 (1 part, by vol., 70%, stock # 33260, Alfa-Aesar) and HCl (3 parts, by vol., -37%, stock # 33257, Alfa-Aesar), poured into the glass cylinder, and allowed to contact the coupon for one hour. Then, the coupon was removed, rinsed, and photographed. The photographs of the tested coupons appear in Figures 3-7.
• compositions that did not perform well against Aqua Regia may perform well in other environments.
• the YSZ coating reduces or prevents coke buildup.
• a composition's performance depends in part on the application and conversion conditions.
• the Clay composition is expected to perform well if it is applied and converted in a suitable environment, as discussed above.
• Figure 8 shows a TEM micrograph at approximately two million x magnification of a stainless steel SS304 substrate (104) having eight coats of an yttria/zirconia composition (102).
• the figure illustrates a diffused coating, labeled Oxide-To- Substrate Interlayer (106).
• the diffused coating is about 10 nm thick.
• the TEM also shows crystal planes, indicating the nanocrystalline nature of the yttria/zirconia.
• the composition is applied to the boiler tubes by inserting a first pig into the boiler tube, adding an aliquot of the composition to the tube, and placing a second pig so that the first pig and second pig substantially contain the aliquot. Then, compressed nitrogen is introduced behind the second pig and the pressure is increased above 1 atm until the pigging package moves. A steady pressure is maintained until the pigging package emerges out the other side of the boiler, and the interior surface of the tube is wetted with the composition. Steam at 500 0 C heats the boiler in the usual manner for 30 minutes, and then the boiler is allowed to cool. A substantially non-porous cerium oxide coating stabilized by chromium oxide forms on the oil-contacting surfaces of the boiler. Example 4
• the cleaned milk-contacting surfaces of a milk pasteurizer are wetted with a well-stirred composition containing titanium(IV) ethoxide in ethanol (500 g, 20 % Ti, Aldrich) and dry ethanol (500 g), using a pig as shown in Figure 1.
• dry nitrogen heated to 450 0 C flushes through the pasteurizer for fifteen minutes, and the pasteurizer is allowed to cool under a flow of room-temperature nitrogen. Analysis will reveal a titanium dioxide coating on the milk-contacting surfaces of the pasteurizer.
• Example 5 A clean automobile exhaust manifold is dipped in a stirred bath containing a first composition that contains zirconium(IV) 2,2,6,6-tetramethyl-3,5-heptanedionate (459 g), yttrium(III) 2,2,6,6-tetramethyl-3,5-heptanedionate (72.9 g), and hexanes (to 1 kg) so the composition contacts interior and exterior surfaces.
• openings can be plugged so the first composition does not contact the interior surfaces.
• the manifold is removed from the composition, suspended, and rotated to allow excess composition to drip into the bath.
• Microwave radiation irradiates exterior surfaces for ten minutes, and an yttria-stabilized zirconia coating forms on the exterior of the manifold.
• the exhaust-contacting surfaces of the manifold are flushed with a second composition containing zirconium(IV) 2,2,6,6- tetramethyl-3,5-heptanedionate (459 g), yttrium(III) 2,2,6,6-tetramethyl-3,5-heptanedionate (72.9 g), platinum(II) acetylacetonate (1.01 g), and hexanes (to 1 kg), and the composition is drained from the manifold.
• Argon gas heated to 450 0 C is passed through the interior of the manifold for 30 minutes. Then, argon gas containing 7 % hydrogen heated to 350 0 C passes through the interior of the manifold for 30 minutes.
• An yttria-stabilized zirconia coating will form on the interior surface of the manifold. The interior surface also will contain platinum metal sites to catalyze the oxidation of partially-combusted hydrocarbon fuel. Moreover, an yttria-stabilized zirconia coating will form to protect the exterior of the manifold from corrosion.
• the manifold can be cooled to room temperature and then slowly lowered into a liquid nitrogen bath for a time.
• the pipes to be treated contained variable inner diameters ranging from 3" to 4", and also included "mule ears," 90° intersections of one pipe entering another. Mule ears provide a particular challenge to certain rigid body pigs, rendering some systems very difficult to send a pig through.
• a receiving pig launcher was attached, and a hose was arranged to pass any fluid effluent (gas and/or liquid) through a water trap which vented to atmosphere.
• the pig launcher with the soaked sponge was sealed, and compressed air from a compressor capable of 160 to 1600 cfm volume and 60 to 150 psi pressure drove the soaked sponge from the pig launcher, through the pipes, and into the receiving pig launcher, at a velocity ranging from 20 to 125 feet per second.
• the pipe was sealed and purged with nitrogen gas.
• the coker burners were turned on one-by-one as is customary for the coker to avoid heating the pipes too quickly, at a maximum heating rate of 250 °F per hour to 820 to 1100 °F maximum temperature. Then the burners were turned off one-by-one to cool the coker slowly to protect the pipes, again in the customary way.

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