DK178004B1 - On-site drying and curing of paint systems using catalytic infrared radiators - Google Patents
On-site drying and curing of paint systems using catalytic infrared radiators Download PDFInfo
- Publication number
- DK178004B1 DK178004B1 DKPA201270268A DKPA201270268A DK178004B1 DK 178004 B1 DK178004 B1 DK 178004B1 DK PA201270268 A DKPA201270268 A DK PA201270268A DK PA201270268 A DKPA201270268 A DK PA201270268A DK 178004 B1 DK178004 B1 DK 178004B1
- Authority
- DK
- Denmark
- Prior art keywords
- coating system
- protective coating
- site
- curing
- emitting unit
- Prior art date
Links
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 47
- 238000001035 drying Methods 0.000 title claims abstract description 16
- 239000003973 paint Substances 0.000 title description 9
- 239000011253 protective coating Substances 0.000 claims abstract description 55
- 238000000034 method Methods 0.000 claims abstract description 54
- 238000000576 coating method Methods 0.000 claims abstract description 53
- 230000005855 radiation Effects 0.000 claims abstract description 28
- 230000001678 irradiating effect Effects 0.000 claims abstract description 5
- 229930195733 hydrocarbon Natural products 0.000 claims description 8
- 150000002430 hydrocarbons Chemical class 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 6
- 239000004215 Carbon black (E152) Substances 0.000 claims description 5
- 239000000446 fuel Substances 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000007605 air drying Methods 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 4
- 239000004567 concrete Substances 0.000 claims description 3
- 238000009423 ventilation Methods 0.000 claims description 3
- 238000007084 catalytic combustion reaction Methods 0.000 claims description 2
- 239000002131 composite material Substances 0.000 claims description 2
- 239000004033 plastic Substances 0.000 claims description 2
- 229920003023 plastic Polymers 0.000 claims description 2
- 230000008569 process Effects 0.000 claims description 2
- 239000002023 wood Substances 0.000 claims description 2
- 239000011248 coating agent Substances 0.000 abstract description 46
- 238000010276 construction Methods 0.000 abstract description 15
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 36
- 239000010410 layer Substances 0.000 description 31
- 229910000831 Steel Inorganic materials 0.000 description 8
- 239000010959 steel Substances 0.000 description 8
- 238000005260 corrosion Methods 0.000 description 7
- 239000003054 catalyst Substances 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 5
- 239000000758 substrate Substances 0.000 description 5
- 239000012855 volatile organic compound Substances 0.000 description 5
- 239000011247 coating layer Substances 0.000 description 4
- 150000002118 epoxides Chemical class 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 231100001010 corrosive Toxicity 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 229920002635 polyurethane Polymers 0.000 description 3
- 239000004814 polyurethane Substances 0.000 description 3
- 230000008439 repair process Effects 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 2
- 239000002519 antifouling agent Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000013521 mastic Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000003039 volatile agent Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- 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
- B05D3/02—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 baking
- B05D3/0254—After-treatment
- B05D3/0263—After-treatment with IR heaters
-
- 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
- B05D5/00—Processes for applying liquids or other fluent materials to surfaces to obtain special surface effects, finishes or structures
- B05D5/005—Repairing damaged coatings
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/02—Heating arrangements using combustion heating
- F26B23/022—Heating arrangements using combustion heating incinerating volatiles in the dryer exhaust gases, the produced hot gases being wholly, partly or not recycled into the drying enclosure
- F26B23/024—Heating arrangements using combustion heating incinerating volatiles in the dryer exhaust gases, the produced hot gases being wholly, partly or not recycled into the drying enclosure by means of catalytic oxidation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/04—Heating arrangements using electric heating
- F26B23/06—Heating arrangements using electric heating resistance heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/28—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
- F26B3/30—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements
- F26B3/305—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements the infrared radiation being generated by combustion or combustion gases
-
- 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
- B05D2202/00—Metallic substrate
- B05D2202/10—Metallic substrate based on Fe
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/006—Removable covering devices, e.g. pliable or flexible
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31511—Of epoxy ether
- Y10T428/31515—As intermediate layer
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Sustainable Development (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
Description
ON-SITE DRYING AND CURING OF PAINT SYSTEMS USING CATALYTIC INFRARED RADIATORS
Technical field of the invention
The invention relates to a method for the on-site surface coating of a structure being part of a large construction.
Background
It is common to apply organic coatings to surfaces of large constructions. Often some smaller structures comprised in the construction need surface finishing with paint, for example the window frames in a building or metal structures comprised in a ship may need anti-corrosion coatings for both protective and aesthetical reasons. These applications or paint jobs can be troublesome, inconvenient and lengthy, because of for example changing weather conditions, the time during which the particular structure cannot be used and, if more than one layer of paint has to be applied, the drying time for each layer, before the next layer can be applied. WO 2011/100970A2 discloses a heater for generating heat by catalytic oxidation of gaseous hydrocarbon. Such heaters may be able to supply infrared radiation to a coated surface, thereby accelerating the curing of a particular type of coating, for example inside a tank. An arrangement of such heaters is shown to be efficient in curing paint applied to the inner side of a tank, in particular a separation tank of an oil production facility. The operation requires careful control of the environment inside the tank, such as for example fresh air supply, temperature, and moisture. A system of heaters adapted for the particular dimensions and geometry of the inner surface of the tank by fastening- and suspension means is provided to ensure adequate curing of the coating applied. The heater system is able to move in a rotational manner when the actuators of the system are switched on.
There remains a need to more conveniently solve such tasks minimizing the drawbacks of such organic coating applications, especially when working in outdoor environments.
Summary of the invention
The invention relates to a method for the on-site surface coating of a structure, said structure being part of a construction comprising a plurality of structures, the method comprising the steps of: a) Applying one or more layers of a protective coating system on-site to at least a part of the structure, b) arranging at least one portable gas catalytic infrared emitting unit in a position so that the infrared radiation is adapted for heating the one or more layers of the protective coating system on-site and c) accelerating the drying and/or curing of the one or more layers of the protective coating system by irradiating the coated surface with infrared radiation emitted by the at least one gas catalytic infrared emitting unit on-site.
In this context, a plurality of structures refers to sub-structures or units that when assembled make up the construction. For example, a ladder could in this context be a structure and a ship could in this context be the construction. A problem related to the surface coating of a surface on-site is that the drying and/or curing of the coating have to take place at ambient conditions. Depending on the actual weather conditions on-site, the cure of each individual layer of a protective coating system may take long time, in some cases at least a day for each layer. According to the invention this time can be drastically reduced by using the method of the present invention. By using portable gas catalytic infrared emitting units to irradiate the coating layers before the application of each new layer, the time for drying and/or curing of each layer is reduced to minutes. A typical coating system for use as for example a repair coating for metal surfaces will provide adequate protection after curing at various ambient conditions. It has surprisingly been found that the properties of the coating system are significantly improved when using gas catalytic infrared emitting units to cure the coating system. By using the method according to the present invention, the adhesion of the coating system to the substrate may be enhanced and the total coating thickness may be reduced. Even the number of layers to provide the necessary coating system properties may be reduced when compared to the same coating system cured under ambient conditions.
Thus, the method of the present invention can save time, making the inventive surface coating process much more efficient than prior art processes. Also coating material may be saved when compared to prior art methods also implying a reduction in costs and less environmental impact. At the same time improved adhesion compared to the prior art may be achieved, also when using standard coating systems, whereby a significant quality gain is provided by the inventive method. Because of the improved quality, intervals between re-coatings may actually be prolonged, further reducing the overall costs of maintaining a particular surface.
In an embodiment of the invention the method further comprises the step of arranging a portable enclosure on-site around at least a part of the structure.
It may be advantageous to establish an enclosure around the surface to be coated. This enclosure can protect the surface against weather conditions such as wind and rain. Also, the infrared emitting gas catalytic radiators can be arranged inside the enclosure, also protecting these from rain, snow and the like. Furthermore, the enclosure may protect the people applying the protective coating system from the weather conditions on-site.
In an embodiment of the invention said method further comprises the step of removing water from the at least a part of the structure prior to the application of one or more layers of a protective coating system by irradiating at least a part of the structure with infrared radiation emitted by the at least one gas catalytic infrared emitting unit.
Sometimes the weather conditions on-site at the site of protective coating system application are not ideal for paint applications. For example, water from the air may condense on a metal surface which is going to be protected by the protective coating system. In this case it may be very advantageous to use the infrared radiation from the gas catalytic infrared emitting unit or units to very efficiently remove the water from the metal surface, before the coating system is applied. Water will absorb the infrared radiation, typically having wavelengths between 1 and 10 pm and simply evaporate from the surface. In this way, a comparatively dry surface more suitable for applying the protective coating system is obtained.
In an embodiment of the invention said surface coating is part of a maintenance procedure.
Larger constructions cannot easily be moved and often must be maintained on-site. By use of the inventive method, the quality and speed of the maintenance procedure may be greatly enhanced.
In an embodiment of the invention said protective coating system is applied as a repair coating.
In connection with repairs, the structure, where a part has been changed or welding has been taking place, must be surface finished to protect the newly installed part or parts from for example corrosion. On offshore constructions the closeness of seawater creates a demanding environment for metals and other construction materials such as concrete. Therefore a protective coating system may advantageously be applied to the part of the structure that has been repaired.
In an embodiment of the invention said construction is selected from the group consisting of an offshore installation, a petrochemical installation, a wind turbine, an oil rig and a ship.
According to preferred embodiments of the present invention, the method can be used on-site on larger constructions that cannot easily be moved to a convenient site for coating application, but a protective coating system is preferably applied on site to a particular structure. Previously, such coating operations were troublesome in that application of a standard protective coating system comprising for example 4 layers: An epoxy primer, 2 layers of epoxy mastic hi-build and a polyurethane topcoat would require approximately three days at a temperature on-site of about 10 °C. At a lower on-site temperature, for example at 5 °C, the time required for applying the above coating system may double, because the time required to cure each layer before it can be painted over with the next layer becomes quite long. It is clear that during this time, the structure being coated cannot be fully used. The costs involved in establishing adequate protection and safety around the structure or part of a structure which is coated may be high. By using the method disclosed herein, the time required to finish the application of the same protective coating system may be reduced to for example one hour, independent on the ambient temperature. Furthermore, in some cases, because of the better cure induced through the use of the inventive method, fewer coating layers may be required to achieve the same or better protection, whereby the time required may be further reduced and material costs decrease considerably.
It is clear that by going from several days to hours in order to finish the whole operation of applying and fully curing a protective coating system on-site, overall costs are significantly reduced. By applying the inventive method on large constructions like oil rigs or ships, the overall savings may be substantial and amount to millions of dollars.
In an embodiment of the invention said protective coating system has anti-corrosion properties.
In advantageous embodiments of the present invention, the protection against corrosion of structures comprised in a construction may be very efficiently performed using the method described herein. This is particularly important when the site of the construction is in corrosive environments such as a site off shore or near seawater, or when corrosive chemicals are used at the site, for example at an oil refinery.
In an embodiment of the invention said protective coating system comprises at least two layers.
Especially the dwell time between the applications of individual layers of the protective coating system may be significantly reduced when using the method of the present invention.
In this respect, the inventive method is particularly advantageous when several coating layers are required. Also layers of substantial thickness may be quickly dried and cured by using the method described herein.
In an embodiment of the invention said protective coating system comprises epoxides.
Most standard protective coating systems for demanding applications comprise binders based on epoxides. It has been found that the inventive method is very suitable for curing such coatings. The formation of cross-links in such coatings is normally around 70% of the theoretical yield, when cured under ambient conditions. By using the method of the present invention, the crosslinks formed may be as high as 80% or 90% such as 95% of those theoretically possible. This means that a protective coating system comprising epoxides, when applied according to embodiments of the present invention, becomes more dense and impermeable for moisture and other corrosives, whereby a quite surprising gain in overall performance and quality of the protective coating system is achieved.
In an embodiment of the invention said protective coating system comprises polyurethane.
As already mentioned for epoxides, a general improvement in crosslink density may be achieved for cross-linked polyurethanes as well when the application follows the method disclosed herein.
In an embodiment of the invention the portable gas catalytic infrared emitting unit is fueled by gaseous hydrocarbons.
Gaseous hydrocarbons are useful as fuel for the portable gas catalytic infrared emitting unit. A preferred fuel is natural gas providing infrared radiation having wavelengths between 1 and 10 pm that are particularly useful according to embodiments of the present invention.
In an embodiment of the invention the portable gas catalytic infrared emitting unit emits radiation having wavelengths from 1 to 10 pm.
To be particularly efficient in embodiments of the present invention, the portable gas catalytic infrared emitting units may emit wavelengths from 1-10 pm. Wavelengths within this range may effectively interact with the molecules within the protective coating system, whereby fast and efficient drying and curing of the protective coating system is obtained.
Surprisingly, the properties of the cured coating film are improved with respect to both adhesion and cross-link density when compared to the same coating film cured under ambient conditions.
In an embodiment of the invention the portable gas catalytic infrared emitting unit emits radiation having wavelengths from 6 to 8 pm.
Without being bound by any theory, experimental indications suggest that the very fast curing times obtainable according to advantageous embodiments of the present invention are promoted by wavelengths in the range of 6 to 8 pm. Further advantages by using these particular wavelengths in the on-site accelerated cure may be improved adhesion of the protective coating system to the substrate and a larger cross-link density within the coating when compared to the cure of the protective coating system at ambient conditions, for example at 5, 10 or 20 °C.
In an embodiment of the invention the portable gas catalytic infrared emitting unit comprises attachment means.
In preferred embodiments, the portable gas catalytic infrared emitting unit has attachment means so that it can easily be attached to for example a scaffold, to a part of the structure to be coated or to another structure in the proximity of the surface to be coated.
Preferably the attachment means are releasable to facilitate easy attachment and detachment.
Also, the attachment means preferably are adjustable to allow for positioning the infrared emitting units so that the coated surface is effectively irradiated by the emitted infrared radiation, when the infrared emitting unit is turned on.
The attachment means could for example comprise clamps, bolts, screws, magnets or any other suitable means of temporary fixation.
In an embodiment of the invention emissions of volatile organic compounds from the protective coating system are removed by catalytically oxidizing the volatile organic compounds (VOC's) by the catalytic action of the portable gas catalytic infrared emitting unit. A further advantage using the method of the present invention is the safe removal of VOC's which may evaporate from the protective coating system during drying and curing. By the air-flow into the catalytic bed of the infrared emitting unit the VOC's are also moving towards and into the catalytic bed and oxidized more or less completely to carbon dioxide.
This improves the environment around the site of coating.
In an embodiment of the invention the accelerated curing of the protective coating system is at least 10 times faster when compared to using conventional air curing at ambient conditions.
In an embodiment of the invention the accelerated curing of the protective coating system is between 20 and 200 times faster when compared to using conventional air curing at ambient conditions.
In advantageous embodiments the full cure of the protective coating system may be achieved in fractions of the time required by the curing taking place at ambient conditions. This may be true for many different protective coating systems that require large amounts of volatiles to evaporate from the coating and/or chemical reactions to take place within the coating.
In an embodiment of the invention the irradiation of the protective coating system after application on at least a part of the structure with infrared radiation emitted by the at least one gas catalytic infrared emitting units on-site, improves the adhesion of the protective coating system to the at least part of a structure by at least 10% when compared to using conventional air drying and/or curing at ambient conditions.
In an embodiment of the invention the irradiation of the protective coating system after application on at least a part of the structure with infrared radiation emitted by the at least one gas catalytic infrared emitting units on-site, improves the adhesion of the protective coating system to the at least part of a structure by 3 to 30 MPa when compared to using conventional air drying and/or curing at ambient conditions. Adhesion is a very important property of a coating system. In advantageous embodiments and by using standard coating material, the method provides a way to enhance the adhesion of the coating system to the substrate. This means that durability of the coating may be prolonged resulting in a reduction of maintenance costs.
Testing the adhesion may be done in several ways. In this context, we refer to ISO 4624.
In an embodiment of the invention the structure is made from a material selected from the group consisting of metal, composite, concrete, plastic or wood.
In principle the method of the present invention may be used on any surface and with many different protective coating systems. Even a combination of materials may be suitable substrates for a protective coating system applied according to embodiments of the present invention.
In an embodiment of the invention the structure is made from steel.
In preferred embodiments, the method of the present invention is used with steel as the substrate on which the protective coating system is applied. The steel can be any type of steel, in particular carbon steel or stainless steel.
The invention also relates to a construction having at least one structure treated according to the method of claim 1.
The invention further relates to a portable drier for accelerating the drying and/or curing of the one or more layers of the protective coating system according to the method of claim 1, said drier comprising: at least one portable gas catalytic infrared emitting unit generating infrared radiation by catalytic combustion of gaseous hydrocarbon fuel and a portable enclosure for enclosing the at least part of a structure and the at least one catalytic radiator. A portable catalytic drier using gaseous hydrocarbon fuel to catalytically generate infrared radiation is particularly useful for the on-site curing of a protective paint system.
The dimensions of the gas catalytic infrared emitting unit are preferably kept comparatively small to ensure easy portability. Typically, the IR-emitting surface of the IR-emitting unit measures between 5 and 30 cm in length and width, while the height would typically be between 4 and 15 cm. Each IR-emitting unit is preferably adapted for easy mounting on a scaffold or other suitable places near the site of use. For example, a steel rod extending vertically from the back of the IR-emitting unit may be used to attach the unit to a scaffold via a clamp arrangement.
The site of applying the protective coating system and curing it by the aid of infrared radiation from at least one portable gas catalytic infrared emitting unit is in certain embodiments of the invention enclosed inside a portable enclosure.
The portable enclosure ensures the protection of the coated surface from for example rain or snow while the coating and curing is taking place.
In an embodiment of the invention the portable enclosure comprises a scaffold and a tarpaulin.
The portable enclosure is in preferred embodiments of the invention built from a scaffold and a tarpaulin. This type of enclosure is versatile, can be built in suitable sizes and provides adequate protection of the site of coating and curing. Furthermore, when packed for transportation, such an enclosure may be small in size and thus well portable.
In an embodiment of the invention said portable enclosure is adapted for ventilation by air, whereby a positive pressure inside the housing can be established.
When working on-site in environments, where there is a risk of accumulating gasses that may bum or explode when in contact with hot surfaces or infrared radiation, it may be important to ventilate the site where the inventive method is applied. This may typically be done by supplying fresh air to the enclosure comprising the gas catalytic infrared radiators in an amount large enough to uphold a positive pressure inside the enclosure.
This may be important for example in connection with applications of the inventive method on an oil production platform, where it also may be necessary to install gas detectors to ensure that both the input of air into the enclosure and the output of air from the enclosure does not contain gas above a threshold limit.
In an embodiment of the invention 1 to 4 of said gas catalytic infrared emitting units can be fitted into a trunk measuring 60 x 40 x25 cm.
In an embodiment of the invention the gas catalytic infrared emitting units can conveniently be transported to the on-site place of application in standard trunks. In this way, a good portability may be facilitated and good protection of the units during transportation may be achieved. The size of the gas catalytic infrared emitting units may thus in preferred embodiments be comparatively small so that 2 or 3 units can be fitted into a standard trunk.
Detailed description
Embodiments of the present invention are now further explained with reference to drawings and examples.
Drawings
Figure 1: Outline of a gas catalytic infrared emitting unit.
Figure 2: Outline of a portable dryer set up for an on-site drying and curing application.
Figure 1 shows an example of a portable gas catalytic infrared emitting unit (8). Infrared radiation is emitted from the front surface (1). A catalyst pad (2) is positioned behind the front surface. A layer of heat insulating material (3) is positioned beneath the catalyst pad (2). Tubing (4) is arranged for supplying and distributing a gaseous hydrocarbon within the catalyst pad.
The unit further comprises a back surface (5) and an enclosure (6). A rod (7) is fitted to the back surface (5) for easy mounting of the unit to a scaffold or the like. A typical unit according to preferred embodiments of the invention may have the following dimensions: The height of the enclosure (6): 7 cm, the width of the front surface: 12 cm and the length of the front surface: 24 cm.
These dimensions are not critical and may be adapted to a certain application. Nevertheless, the units should be kept a size which facilitates portability.
The units may also comprise means for electrical pre-heating of the catalyst pad.
Gas is then supplied to the preheated catalyst pad and the hydrocarbons are catalytically oxidized maintaining the catalyst at working temperature and emitting infrared radiation from the front surface.
Gas catalytic heaters and modules are commercially available from a number of sources.
Figure 2 shows an example of a portable drier used on-site according to an embodiment of the present method. A gas catalytic infrared emitting unit (8) is attached inside a portable enclosure (13), for example a tent or a scaffold equipped with a tarpaulin. A fan (9) provides an air flow into the enclosure through a hose (10) establishing a positive pressure inside the enclosure. The enclosure is situated inside a classified area indicated by the dotted line (12) while the air for ventilation is provided from a non-classified area. The classification may for example relate to a risk of leaks of substantial amounts of natural gas on an oil rig. There therefore could be a risk of explosion. A gas detector (11) is mounted both in the air supply hose and in the enclosure. An entrance (14) to access or leave the enclosure allows personnel to access the site of application of the protective paint system. Setting up the portable IR-units, given that a portable enclosure like the one outlined on figure 2 has been established on for example an oil rig, can be done for example within one hour.
The method of applying the protective coating system is not critical. Application may be with a brush, by spraying or any other known method.
The time required to perform the full coating operation depends on the particular coating system and the number of layers required.
Previously, when using ambient conditions to cure a coating system approved for use for demanding applications such as on an oil rig, restricted access to the area around the coated structure had to be established for several days, depending on the exact weather conditions such as the temperature. In cold environments (around 5 °C ambient temperature), proper cure of a layer could take for example 2 days before the next layer can be applied. Thus, for a 4-layer coating system, 8 days could be required before the area affected by the coating operation could be fully accessed again.
By using an installation as illustrated on figure 2, the same 4-layer coating system can be applied and fully cured within hours, such as for example 1 or 2 hours, or even faster.
The IR-units heat each coating layer to a temperature of for example 80 °C and keep the layer at that temperature for about 5 minutes. The surface is then allowed to cool to a temperature of about 50 °C, before the next layer is applied, heated and so on. When the last layer has been kept at about 80 °C for about 5 minutes, the whole operation is ended, the portable drier can be packed and a new coating operation can be initiated at some other site.
The savings involved by using the arrangement on figure 2 on for example an oil rig or a ship may be substantial.
Clearly the fan, hose and gas detectors indicated on figure 2 may not be necessary if there is no risk for large amounts of for example inflammable substances to reach the IR-units.
Examples
The following example illustrates some of the benefits which may be achieved according to an embodiment of the present invention.
The data given in Table 1 reflect an example for an offshore application where part of a structure of steel has to be protected against corrosion on an oil rig. The procedure when using IR reflects a setup as described on Figure 2.
Table 1. Comparison of the procedure for a standard offshore on-site coating application with an application using the method comprising the step of curing the paint system by using portable gas catalytic infrared emitting units.
While the standard offshore procedure requires curing at ambient conditions, here 10 °C, the procedure when using IR requires the paint film to absorb infrared radiation until a temperature of about 80 °C is reached and kept for about 5 minutes, where after the painted surface is allowed to cool to 50 °C. The time required for the cooling step is taken account of in Table 1 in that approximately 30 minutes are required, before the next layer of coating can be applied.
Both procedures in Table 1 result in a coated steel surface giving a specified corrosion resistance. Evidently the performance of the IR-cured coating is better with respect to adhesion and only a two-layer system is necessary to achieve the desired corrosion resistance.
Also it is evident that the time required before the steel structure is protected and accessible for use is far less for the method using gas catalytic infrared emitting units for accelerated IR-cure.
Claims (8)
1. Fremgangsmåde til overfladebelægning på stedet af en struktur, idet strukturen er del af en konstruktion, der omfatter en flerhed af strukturer, hvilken fremgangsmåde omfatter trinnene: a) påføring af et eller flere lag af et beskyttende belægningssystem på stedet på i det mindste en del af strukturen, b) anbringelse af mindst én bærbar gaskatalytisk infrarødsemitterende enhed i en position, således at den infrarøde stråling indrettes til at opvarme det ene eller de flere lag af det beskyttende belægningssystem på stedet, og c) accelerering af tørringen og/eller hærdningen af det beskyttende belægningssystems ene eller flere lag ved at bestråle den belagte overflade med infrarød stråling, der emitteres fra den mindst ene gaskatalytiske infrarødsemitterende enhed på stedet, hvor fremgangsmåden yderligere omfatter trinnet til anbringelse af et bærbart indelukke på stedet omkring i det mindste en del af strukturen for at beskytte den i det mindste ene del af strukturen imod vejrforhold, hvor mindst to lag af det beskyttende belægningssystem påføres, og hvor konstruktionen er en petrokemisk installation.
2. Fremgangsmåde ifølge krav 1, hvor fremgangsmåden yderligere omfatter trinnet til fjernelse af vand fra den i det mindste ene del af strukturen inden påføringen af et eller flere lag af et beskyttende belægningssystem ved at bestråle i det mindste en del af strukturen med infrarød stråling, der emitteres fra den mindst ene gaskatalytiske infrarødsemitterende enhed.
3. Fremgangsmåde ifølge et hvilket som helst af kravene 1-2, hvor den bærbare gaskatalytiske infrarødsemitterende enhed emitterer stråling med bølgelængder på fra 6 til 8 pm.
4. Fremgangsmåde ifølge et hvilket som helst af kravene 1-3, hvor den accelererede tørring og/eller hærdning af det beskyttende belægningssystem er mellem 20 og 100 gange hurtigere sammenlignet med anvendelse af konventionel lufttørring og/eller hærdning under omgivende forhold.
5. Fremgangsmåde ifølge et hvilket som helst af kravene 1-4, hvor bestrålingen af det beskyttende belægningssystem, efter påføring på i det mindste en del af strukturen, med infrarød stråling emitteret fra den mindst ene gaskatalytiske infrarødsemitterende enhed på stedet forbedrer adhæsionen af det beskyttende belægningssystem til den i det mindste ene del af strukturen med mindst 10 % sammenlignet med anvendelsen af konventionel lufttørring og/eller hærdning under omgivende forhold.
6. Fremgangsmåde ifølge et hvilket som helst af kravene 1-5, hvor strukturen er fremstillet af et materiale udvalgt fra gruppen bestående af metal, komposit, beton, plast eller træ.
7. Bærbart tørringskit til accelerering af tørringen og/eller hærdningen af det beskyttende belægningssystems ene eller flere lag ifølge fremgangsmåden ifølge krav 1, hvilken tørrer omfatter: mindst én bærbar gaskatalytisk infrarødsemitterende enhed, der genererer infrarød stråling ved hjælp af katalytisk forbrænding af gasformig carbonhydridbrændstof og et bærbart indelukke til indelukning af den i det mindste ene del af strukturen og den mindst ene katalytiske strålingsenhed.
8. Fremgangsmåde ifølge et hvilket som helst af kravene 1-6 eller tørringskit ifølge krav 7, hvor det bærbare indelukke er indrettet til luftventilation, hvorved der kan etableres et positivt tryk inde i huset.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DKPA201270268A DK178004B1 (en) | 2012-05-21 | 2012-05-21 | On-site drying and curing of paint systems using catalytic infrared radiators |
EP13725560.0A EP2852800A1 (en) | 2012-05-21 | 2013-05-21 | On-site drying and curing of paint systems using catalytic infrared radiators |
PCT/DK2013/050151 WO2013174383A1 (en) | 2012-05-21 | 2013-05-21 | On-site drying and curing of paint systems using catalytic infrared radiators |
US14/403,104 US20150128443A1 (en) | 2012-05-21 | 2013-05-21 | On-Site Drying And Curing Of Paint Systems Using Catalytic Infrared Radiators |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DK201270268 | 2012-05-21 | ||
DKPA201270268A DK178004B1 (en) | 2012-05-21 | 2012-05-21 | On-site drying and curing of paint systems using catalytic infrared radiators |
Publications (2)
Publication Number | Publication Date |
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DK201270268A DK201270268A (en) | 2013-11-22 |
DK178004B1 true DK178004B1 (en) | 2015-02-23 |
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DKPA201270268A DK178004B1 (en) | 2012-05-21 | 2012-05-21 | On-site drying and curing of paint systems using catalytic infrared radiators |
Country Status (4)
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US (1) | US20150128443A1 (da) |
EP (1) | EP2852800A1 (da) |
DK (1) | DK178004B1 (da) |
WO (1) | WO2013174383A1 (da) |
Families Citing this family (3)
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GB2539939A (en) * | 2015-07-01 | 2017-01-04 | Agv Tech Ltd | Drying method |
US10532315B1 (en) | 2015-08-27 | 2020-01-14 | Advanced Catalyst Systems Llc | System for flameless catalytic destruction of fugitive organics and producing environmentally clean hot gas for other uses of thermal energy |
CN115404121A (zh) * | 2022-07-28 | 2022-11-29 | 江苏科技大学 | 一种藜麦油的加工方法 |
Citations (4)
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US20110064888A1 (en) * | 2009-09-11 | 2011-03-17 | Whitley Jeffery G | Portable heating apparatus for powder coating |
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WO2012012865A1 (en) * | 2010-07-29 | 2012-02-02 | 9227-5668 Quebec Inc. | Portable catalytic heating apparatus for drying, curing, polymerization or cross-linking of coatings and compounds |
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US3559280A (en) * | 1968-03-13 | 1971-02-02 | Allied Tube & Conduit Corp | Method and apparatus for the continuous forming, galvanizing and coloring of tubing |
GB1310425A (en) * | 1970-07-28 | 1973-03-21 | Blundell Permoglaze Ltd | Stoving painted or lacquered articles |
US3652485A (en) * | 1970-10-13 | 1972-03-28 | Us Navy | Aircraft carrier deck coating nasl-c-1230 |
DE3819294A1 (de) * | 1988-06-07 | 1989-12-14 | Heinrich Prof Dr Ing Reents | Verfahren mit den dazugehoerigen vorrichtungen zur trocknung bzw. erwaermung von flexiblen oder festen koerpern mit hilfe flexibler, leicht ortsveraenderbarer luftkammern bei gleichzeitiger abfuehrung des kondensates |
US5355823A (en) * | 1991-10-24 | 1994-10-18 | Mmc Compliance Engineering, Inc. | Apparatus and method for performing external surface work on ships' hulls |
US5832859A (en) * | 1996-01-17 | 1998-11-10 | Newport News Shipbuilding And Dry Dock Company | Welded stud hanging assembly for a blasting and coating containment system |
US5885154A (en) * | 1997-06-17 | 1999-03-23 | Napadow; Michael F. | Air supply means for a controlled environment room |
US6455817B1 (en) * | 2001-08-22 | 2002-09-24 | The Boeing Company | Structure for housing a workpiece during curing and associated method |
CN101336352A (zh) * | 2006-01-26 | 2008-12-31 | 热传动装置专业有限责任公司 | 用于离网应用的可携带催化加热系统 |
US8735512B2 (en) * | 2008-04-09 | 2014-05-27 | Air Products And Chemicals, Inc. | Curing agent for low temperature cure applications |
ES2363895B1 (es) * | 2008-08-04 | 2012-07-04 | Roisber Servicios, S.L | Cabina de pintura movil |
DE102010050704A1 (de) * | 2010-11-03 | 2012-05-03 | Gerd Wurster | Verfahren und Vorrichtung zum Beschichten von langen Bauteilen |
-
2012
- 2012-05-21 DK DKPA201270268A patent/DK178004B1/da not_active IP Right Cessation
-
2013
- 2013-05-21 US US14/403,104 patent/US20150128443A1/en not_active Abandoned
- 2013-05-21 WO PCT/DK2013/050151 patent/WO2013174383A1/en active Application Filing
- 2013-05-21 EP EP13725560.0A patent/EP2852800A1/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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US5586877A (en) * | 1995-07-20 | 1996-12-24 | A.J.C. | Infrared ray emitters with catalytic burner |
US20110064888A1 (en) * | 2009-09-11 | 2011-03-17 | Whitley Jeffery G | Portable heating apparatus for powder coating |
WO2011100970A2 (en) * | 2010-02-16 | 2011-08-25 | Netek Ir System A/S | A heating system |
WO2012012865A1 (en) * | 2010-07-29 | 2012-02-02 | 9227-5668 Quebec Inc. | Portable catalytic heating apparatus for drying, curing, polymerization or cross-linking of coatings and compounds |
Also Published As
Publication number | Publication date |
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US20150128443A1 (en) | 2015-05-14 |
EP2852800A1 (en) | 2015-04-01 |
DK201270268A (en) | 2013-11-22 |
WO2013174383A1 (en) | 2013-11-28 |
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