CA2147479A1 - Process for the production of a powder coating, apparatus for carrying out the process, and powder formulation for carrying out the process - Google Patents

Abstract

The present invention relates to a process for the production of a powder coating, in which a suspension of powder particles is sprayed and the spray jet is directed onto the substrate to be coated, characterized in that 1.) a suspension of powder particles in a liquefied gas is employed, the gas having been liquefied under under [sic] a pressure of not more than 20 bar, and 2.) the liquid gas is vaporized before, during or after the spraying of the suspension.

Description

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l~*T TRANSLATION

PAT 93 394 September 20, 1993 BASF Lacke + Farben Aktiengesellschaft, Munster Process for the production of a powder coating, apparatus for carrying out the process, and powder formulation for carrYinq out the process The invention relates to the powder coating of, in particular, thin-walled metal components of large surface area, and above all car bodies.
For a wide variety of areas of application, pulverulent substances are required which have extremely low particle sizes of less than about 20 ~m.
It is frequently problematic in the case of fine-particled powders of this type that these materials aredifficult to handle and, in particular, problems occur with respect to their flowability. Another particular problem is the production of coatings using these fine-particled powders. One example of such an area of application is the sector of catalyst technology, in which the active substances, in addition, have to be introduced into fine pores in the support materials.
A further important area of application for fine-particled pulverulent substances is that of powder coatings, which are gaining increasing importance.
Conventional cozting procedures, in which colored pigment particles dispersed in a conventional liquid solvent are sprayed in the form of paint droplets onto the components to be coated, represent 21~7179 considerable environmental pollution because of the contamination of the exhaust air, which is concentrated during, for example, the line production of passenger cars.
5In the interests of improved environmental protection, three kinds of coating have been developed for more environmentally friendly spray coating (R. Laible, Umweltfreundliche Lackiersysteme fur die industrielle Lackierung [Environmentally Friendly 10Coating Systems for Industrial Coating], Expert Verlag, Esslingen, 1988), namely high-solids coatings, water-borne coatings and powder coatings.
High-solids coatings are essentially none other than normal coatings which have been thickened; in 15other words, the emissions into the surrounding air of solvents of which some are harmful are reduced, but not eliminated. Waterborne coatings have the disadvantage that the overspray in the water has to be recovered.
Powder coatings lead neither to significant 20contamination of the air nor to polluting contamination of water. In its current state of development, however, this process has a number of disadvantages which stand in the way of its broad application, especially in the sector of the thin coating of thin metal components of 25large surface area, for example vehicle bodies.
The principle of electrostatic powder coating, which has been introduced since 1965, is very simple. A
powder coating comprises particles of colored powder dispersed in air which have a particle-size range of 2147~9 from 20 - 60 ~m with average particle sizes of from 40 -50 ~m. When dispersed in air (fluidized), such powder coating particles have the flow characteristics of a fluid. This property is the reason why they can be used in spray painting. They are charged in special electrostatic spray guns and sprayed onto an earthed workpiece to which they adhere electrostatically.
Particles of powder coating which have been sprayed past the workpiece and have not been deposited are suctioned off, separated from the air, screened and re-used.
The advantages of powder coating are consequently that virtually no environmental pollution occurs and that the utilization of material which can be achieved, by dry suction and separation, is very good, since overspray is recovered without troublesome residues.
The ability to utilize this powder coating technology is, however, restricted to the application of relatively thick coats of at least 70 ~m since, in order to have a smooth surface, the coat must be at least about 70 ~m thick, and it is not possible to process relatively fine particles using this process without encountering problems.
Known powder coatings belong to a class of bulk material which is capable of holding air. Its characteristics are as follows: a bed of particles of material - cracking catalysts being a typical example -expands on fluidization (fluidized bed) distinctly .

above the m; nimllm fluidization, before air bubbles start to form in the fluidized bed. If the supply of air is cut off suddenly, then the bed collapses slowly at a rate of from 0.3 - 0_6 cm/s, corresponding to the empty-tube velocity in the suspension phase.
A type of bulk material comprising particles below about 20 ~m, which includes materials which are noticeably cohesive, i.e. in which the adhesive forces between the particles significantly exceed the other possible forces in the fluidized bed, namely weight and flow resistance, permits more or less poor fluidization only with the additional use of, for example, mechanical stirrers, although hardly achieving true dispersion of the particles.
Powder coatings have a solids density of about 1500 kg/m3. At atmospheric pressure, the density of air is negligible. Only a particle-size distribution of the powder coatings within the range between 20 ~m and 60 ~m guarantees that powder coatings will be in the region of the excellent fluidization properties required. The consequence of this lower particle-size limit is, therefore, that it is not possible to go below certain minimum layer thicknesses, and that high surface quality, leveling and gloss are only achieved at layer thicknesses > 70 ~m, i.e. with high paint consumption and thick coats of paint.
A significantly broadened range of applications for the known powder coating technology in order to give thinner coatings of high quality would necessitate -powder coating particles of an unsuitable bulk material type cont~in;ng particles below about 20 ~m. Prior-art powder coating technology is therefore denied access on physical grounds to desirable low particle size ranges.
Important areas of application - for example catalyst production, in which the active substance is introduced into the pores of a support substance - are also closed to this technology.
Moreover, present-day powder coating technology is restricted to a number of selected binder/cùring agent systems because, for example, reactive systems are not accessible to powder coating technology. For instance, it is not possible to formulate powder coatings as two-component systems in which the curing agent and the binder are stored separately and are mixed only shortly before application. In fact, to obtain homogeneous powder coatings, specific process steps are necessary in the production of the powder coatings. Conventionally the powder coating is first extruded and is only then ground, so as to guarantee a homogeneous distribution of the individual components of the powder coating. In contrast, it is not possible to produce a powder coating having homogeneous distribution of the individual components simply by dispersing them.

Consequently, it is not possible to produce powder coatings at the actual premises of the user from a binder component and a curing-agent component. It is - 2147~79 -for this reason that it is not possible to formulate powder coatings which contain components which are reactive at ambient temperature, for example OH group-contA;ning binders and curing agents which are reactive at ambient temperature and are based on free isocyanate groups.
In addition, the extrusion step which is necessary in the conventional processes for the production of powder coatings is time-consuming and cost-intensive. Furthermore, in the case of reactive systems, t is quite possible for problems to occur during extrusion (premature reaction), once again necessitating appropriate and laborious measures.
A further reason why powder coating technology is restricted to a number of selected binder/curing agent systems is that the present-day powder coatings must have glass transition temperatures Tg of > 40C, so as to ensure the resistance to agglomeration of the powder coatings. Indeed, the powder coatings are in general capable of being stored at ambient temperature (generally 25C) and of remaining free-flowing if the glass transition temperature of the powder coatings is above the ambient temperature.
EP-A-421796 discloses a process and a device for the spray application of liquid coating compositions which comprise supercritical or liquefied gas. In this context it is essential to the invention to employ a specially constructed spray nozzle in AMENDED SHEET

2147~79 order, for example, to avoid losses of the supercritical or liquefied gas.
The technical problem on which the invention is based, starting from the fact that powder coating represents the only truly environmentally friendly coating process, and in view of the above-described limitation of present-day powder coating technology, is to broaden the scope of application of powder coating technology. Hence it should also be possible to produce relatively thin coatings with a very high surface quality and hiding power in combination with perfect leveling and gloss, without causing any new kind of environmental pollution. In addition it is intended to provide powder coatings based on an e~pAn~ed range of binder/curing agent. A particular intention is to enable the formulation of powder coatings on the basis of reactive systems, i.e. binder/curing agent systems which are reactive even at ambient temperature.
Finally, it is intended to open up completely new areas of application to powder coating technology, for example the sector of catalyst production.
A process solving this problem is characterized along with developments thereof in the patent claims. Also indicated in the patent claims is a grinding process for the production of the powder to be employed in accordance with the invention, and a powder suspension which is suitable for the powder coating process.

AMENDED SHEET

Finally, the invention relates to the application of this process to the production of catalysts.
It is surprising and was unforeseeable that the suspension of various finely divided materials in gas liquefied under a pressure of not more than 20 bar would give suspensions which permit problem-free management and can be employed in a very wide range of sectors. For instance, the suspension according to the invention in the gas liquefied at a pressure of not more than 20 bar can be employed advantageously for all materials which can readily be suspended in the liquefied gas.
For the production of the suspensions employed in accordance with the invention, all those liquefied gases are suitable which have been liquefied at a pressure of not more than 20 bar, preferably not more than 10 bar and particularly preferably at normdl atmospheric pressure by having been cooled, by methods known to those skilled in the art, to the appropriately low temperatures. Examples which can be mentioned of suitable liquefied gases are liquid nitrogen, liquid air and liquid helium. On account of its ready availability and its low price, liquid nitrogen is employed in particular, although other liquefied ga~es can also be employed depending on the intended use of the suspensions.
The use of gas which has been liquefied at a pressure of not more than 20 bar is [sic] ensures that g the suspension can be managed without complex equipment for maintA;ning high pressures, whereas the use of supercritical gases, for example liquefied C02, requires high pressures to be maintained during preparation, storage, transportation and processing of the suspensions. The use of gases which have been liquefied at a pressure of not more than 20 bar does not, however, of course exclude the possibility that the suspension employed in accordance with the invention is subjected to an elevated pressure, for example during transportation in a closed circular line, it just means that such a pressure is not necessary for maintAin;ng the suspension.
Owing to the low temperatures associated with the use of gas liquefied at a pressure of not more than 20 bar (e.g. -196C for liquid nitrogen at atmospheric pressure), the suspensions according to the invention are suitable in particular for materials which are reactive at ambient temperature and which therefore cannot normally be stored/transported and, in some circumstances, cannot even be processed.
In addition, such suspensions in liquefied gas can be employed advantageously for the production of catalysts, especially organometallic catalysts. In this 25- context the active substance is suspended in the liquefied gas and then introduced into the pores of the support substance, and the liquefied gas is then vaporized. This produces catalysts in which the active substance is deposited uniformly in the pores of the support substance. As is usual in the sector of catalyst production, it is of course necessary in this case too to test the so-called bleeding behavior, i.e.
to ascertain whether the active substance also remains in the pores of the support substance at the reaction temperatures at which the catalyst is used.
The essence of the invention consists in employing a suspension of powder particles, which may also be considerably finer than previously, in a liquefied gas of low viscosity and in heating this suspensior., or at least the liquid-gas fraction, during, before or after spraying, until the quantity of heat or energy available is sufficient to vaporize the liquefied gas during spraying. In this way a flowable and sprayable stable powder suspensions [sic], in particular a powder coating suspension, is provided which is highly suited to storage and transportation and can be sprayed to give thin coatings of high gloss.
The invention is now described below in more detail by way of example, on the basis of the process of powder coating. It is of course also possible to produce other coatings, for example for the production of catalysts, using this process. This applies especially to all sectors in which it is important to produce coatings having an extremely low layer thickness using powders having an average particle size ~ 15 ~m, preferably < 10 ~m. Examples which can be mentioned are the sectors of coating using metals or adhesives, the doping of surfaces, the production of alloys, the coating (antistatic finishing) of films, the coating of ceramics and the coating of structured bodies, fibers or nonwovens.
The preparation of the powder coating suspension can be carried out in well-insulated supply vessels or stirred vessels, which, in order to maintain good heat insulation, advantageously have a stirrer with magnetic drive for repeated suspension. In order, with a level of liquid which decreases during processing, always to maintain an admission pressure of, for example, 5 bar at the coating nozzles, the stirred vessel is provided not only with a heating means but also with a cooling means. Both are connected to a regulating facility.
The processing of the powder coating is carried out in a manner known per se in that the supply vessel or stirred vessel is connected, either directly or via a thermally well-insulated closed circular line, to one or more spray guns: in the latter case, the circulation of the suspension can be carried out via a circulating pump.
Connected to the stirred vessel or to the closed circular line in a manner known per se are, for example, two-fluid or multifluid nozzles for atomizing the suspension. In the prior-art fluid coating of, for example, car bodies, about 20 spray nozzles are provided. With a coating time of 1 minute per body, the necessary throughput through one die is then 100 g/min of powder coating. At a powder coating density of 1500 kg/m3, the result is a powder coating volume flow of vp = 0.067 l/min. In accordance with experience, a suspension with a solids content of 25% by volume can be conveyed very readily. As long as certain m; n; mllm transportation rates are exceeded, an average particle size of the powder coating of 5 ~m prevents sedimentation of the solid. Consequently, the suspension volume flow to be processed per atomizer nozzle is 0.067 x 60 Vsus = = 16 l/h.
0.25 Such atomization capacities can easily be achieved by commercially available two-fluid nozzles for spray painting. Special two-fluid spray guns are therefore not necessary. At a nozzle admission pressure of approximately 4 bar, on both the liquid side and on the gas side, it would be possible to achieve droplet sizes of 30 ~m with water to be atomized. The significantly lower - in comparison to water - viscosity and surface tension of an inert gas, in particular nitrogen, in the vicinity of its boiling point allow smaller droplet sizes to be achieved in comparison with water. A
two-fluid nozzle having the operating data mentioned above requires a gas flow rate of vg = 170 l/min for the atomization of a volume flow of suspension of v sus = 16 l/h. If the paint processor employs heated dry air 21~7479 at 4 bar for this purpose, then the two-fluid nozzle can be operated in accordance with the principle, known from power station engineering, of injection cooling, i.e. the two-fluid nozzle can be operated with atomizer S air which has been heated such that the amount of heat supplied is sufficient for the practically instantaneous vaporization of the solids-containing nitrogen droplets.
In order to vaporize liquid nitrogen (-196C) and to heat it to ambient temperature (25C), a heat supply of 1.2 kW per nozzle is required. This quantity of heat can be supplied by preheating the quantity of gas required for atomization to approximately 150C.
The powder coating/gas flow leaving the nozzle then has a temperature of 25C. Depending on the desired temperature of the powder coating/gas flow, the ga~
employed for atomization can also be heated to other temperatures. The critical factor, however, is in each case the quantity of heat introduced by the gas, which depends not only on the temperature of the atomization gas but also on the respective quantity of ga~.
Advantageous temperatures and gas quantities in each case also depend on the respective powder coating and can be determined on the basis of a few routine experiments.
In addition, however, it may al~o be advantageous to operate the two-fluid nozzle with cooled rather than with heated atomizer air, especially when processing powders which are reactive at ambient - 2147~79 temperature. It is thus also possible to supply the quantity of heat required to vaporize the liquid nitrogen and to heat it to ambient temperature not only by supplying a heated atomizer gas. This quantity of heat can also, of course, be supplied in whole or in part by other methods, for example radiant heating.
It should also be ensured when carrying out the process according to the invention that the dew point of the surroundings is not reached, so as to avoid the formation of ice crystals. This can be effected by appropriate heating, for example to 25C, as is described above. Preferably, however, the coating process according to the invention is carried out in a dry atmosphere (i.e. in an atmosphere having as low as possible an atmospheric humidity). When operating with powder suspensions in liquid nitrogen, powder application is advantageously carried out in a nitrogen atmosphere (in particular, a closed circuit).
The powder coating suspension according to the invention can be applied not only with the commercially available two-fluid nozzle described above but also using a commercially available airless nozzle. In this case it should be ensured by corresponding apparatus, as when employing the two-fluid nozzle and using cooled atomizer air, that the liquid nitrogen is vaporized and heated to ambient temperatures. The quantity of heat required for this can be effected tsic], for example, by means of radiant heating, by means of a heated stream of gas outside the nozzle, or the like.

` - 2147479 At a powder coating density of approximately 1500 kg/m3 and a powder/liquid nitrogen suspension having a solids content of 25% by volume, 2 1 of liquid nitrogen are to be employed per kg of powder coating.
At a bulk purchaser price per liter of DM 0.5/1 for liquid nitrogen, the additional cost of the coating process per kg of powder coating is DM 1.00; the cost at a powder coating price of approximately DM 8.00/kg is therefore a rise in the price of feedstocks by approximately 13%.
The new powder coating process permits the use of known and tried components. The process chain can be divided into three substeps: paint production, storage and transportation, and paint processing.
The powder coating is produced on the basis of known powder coating particles, having an average particle size of, for example, about 40 - 50 ~m. It is, however, also possible to employ powder coatings having markedly greater average particle sizes. This powder is metered from a supply vessel into a mixing vessel and is then suspended in the liquid gas, preferably in liquid nitrogen. As has been ascertained, powder coating particles having an average particle size of 50 ~m can be dispersed in liquid nitrogen with no problems. Paint powder having an average particle size of approximately 50 ~m is thus mixed with liquid nitrogen in a mixer to give a suspension and is then ground finely to the desired particle size. As mentioned, however, it is also possible to suspend powder coatings having a markedly greater particle size and then to grind them to the desired particle size.
Since the liquid nitrogen is in the vicinity of its boiling point of -196C, its viscosity, at 8.9-10 5 Ns/m2 (cf. water at 1.10 3 Ns/m2), is extremely low. When using stirred ball mills for the fine grinding, for example from the companies Draiswerke or Netzsch, the viscosity of the suspension should not exceed 10 Pas. Because of the low viscosity of liquid nitrogen, a comparatively highly concentrated suspension can therefore be employed. Grinding is carried out until the average particle size is less than 15 ~m, preferably from 5 to 10 ~m. The suspension thus ground comprising particles having an average lS particle size of less than 15 ~m, preferably of from 5 ~m to 10 ~m, and liquid nitrogen is then dispensed into thermally well-insulated transportation vessels, which are at the same time the suspension or stirring vessels for redispersion at the premises of the paint processor, and in which the powder coating suspension can also be stored without problems.
In addition, it is also possible to produce the powder coatings by, first of all, adjusting the particle size of the powder coatings (particle size distribution) to the values required, using corresponding grinding equipment, in combination if desired with suitable classifying and screening devices. For example, for the production of powder coatings having a small average particle sizes [sic] of - 21g7479 < 15 ~m, it is possible to employ fluidized-bed ]et mills (AFG) from Alpine, Augsburg, in combination if desired with Turboplex ultrafine classifiers from Alpine, Augsburg. Subsequently, these powder coatings having the desired particle-size distribution are then suspended using appropriate mixers or dispersion equipment in the liquid gas, preferably in liquid nitrogen.
In this context it is advantageous, for example, that the binder and the curing agent can be ground separately and the resulting fine particles can be suspended directly in the liquid gas, in particular in liquid nitrogen. This enables the production of powder coatings without an extrusion step.
Since the suspension of the finely ground particles in the liquid gas can be carried out using simple mixing or dispersion equipment, it is even possible to produce the powder coating suspension prior to application at the actual premises of the respective user. This enables, on the one hand, the use of reactive systems, since this variant permits the formulation of powder coatings as two-component systems. On the other hand, a con~iderable [sic] larger scope is provided for variation with regard, for example, to different shades of color, since the pigments as well, in an appropriately finely ground form, can be added to the powder coating actually on site during the preparation of the suspension. It is also possible to regulate many applications properties 2147~79 of powder coatings by appropriate addition of additives. Because no extrusion cut [sic] is necessary for the homogeneous incorporation of these additives, powder coatings can be produced in practice by the "building-block principle. This means that every user can produce the powder coating which is optimum for their purposes, because the individual components (binders, curing agents, pigments, additives etc.) can be supplied in finely ground form and can be processed actually on site by suspension in liquid gas to give the powder coating. In this way, it is also possible to produce relatively small quantities of a specific powder coating in a cost-effective way. In addition, liquid components (curing agents, additives etc.) can àlso be incorporated into the powder coating without problems in the process according to the invention.
Furthermore, since the powder coating is very simple to suspend because of the low viscosity (and the low surface tension) of the liquefied gas (especially in the vicinity of the boiling point of the liquefied gas), it is also possible to prepare the suspenffion actually in the nozzle. In airless application, this can be carried out u~ing a commercially available two-fluid nozzle. If operating with the use of atomizer air, processing is carried out accordingly by mean~ of a commercially available three-fluid nozzle which is likewise known.
Depending on the system, however, it may under certain circumstances be quite desirable for the powder coating suspension to be prepared not actually at the premises of the particular user, but directly after the preparation of the powder coating components. The storage and transportatio~ of the new powder coating suspension are then carried out expediently in the insulated transportation vessels which are also used by the paint processor as supply and stirring vessels.
Indeed, using this type of storage and transportation, problems in the previous handling of powder coatings are solved at the same time:
Powder coatings contain reactive components which, on being stored for prolonged periods at ambient temperatures, lead to aging of the coating. Because of the low temperature of the powder coating suspension (about -196C), however, no such reaction takes place.
Consequently, it is even possible to formulate powder coatings which contain components which would react directly at room temperature (about 25C), for example powder coatings based on hydroxyl group-contA; n i ng binders and reactive crosslinkers contA; ni ng free isocyanate groups. It is also possible to incorporate sensitive constituents, for example aluminum bronzes, into the powder coating without problems and without expensive protective treatment. By this means, powder coating technology is extended to other binder/curing agent systems which were hitherto inaccessible to it.
Moreover, known powder coatings solidify during prolonged transportation, especially transportation by ship, in such a way that their redispersion becomes practically impossible. With the production and storage of the powder coating as are proposed in this document, it is possible in principle to supply paint processors worldwide from one paint production site. Since it has even been possible, for very large storage quantities, for example liquefied natural gas, to set up a refrigeration chain, it is likewise possible for the considerably smaller quantities of powder coating suspension, for example in the form of suitably designed insulated transportation containers, known as insulated vessels.
Finally, the process according to the invention also makes possible the use of powder coatings which have markedly reduced glass transition temperatures Tg.
Indeed, so that the current powder coatings retain their long-term flowability, the Tg of the powder coatings must usually be > 40C. By contrast, when the powder coating is stored and transported in liquid nitrogen, powder coatings having markedly lower Tg values, for example < 0C, can also be employed. This opens up new spheres of use to powder coatings. In addition, it is also possible by this means to improve the properties of the powder coatings for specific applications. For example, the leveling of powder coatings with a decreasing Tg is improved markedly, which is of importance, for example, for the use of powder coatings in the sector of the topcoat finishing of automobile coaches [sic]. Also possible in this way is the formulation of stone chip-resistant coatings having distinctly improved properties.
On the basis of the abovementioned advantages associated with the use of liquid gas, it is consequently possible to formulate, for example, powder coatings on the following chemical basis:
a) binders contA;ning active hydrogen atoms (e.g.
compounds contAining O~, NH and SH groups), in combination with compounds which contain free isocyanate groups, b) compcunds cont~ining carboxyl groups or amino groups, in combination with compounds contA; n; ng epoxide groups, c) carbodiimide systems, in combination, for example, with compounds contA;n;ng carboxyl or amino groups, d) compounds cont~;n;ng amino groups, in combination with compounds contAin;ng carbonate groups, e) systems which cure by the principle of Michael Addition, for example compounds cont~;ning an activated double bonds [sic], in combination with compounds cont~;n;ng active hydrogen, f) binders cont~; n; ng active H atoms, in combination with anhydride systems, g) moisture-curing systems and h) powder coating systems already in general use.
Finally, the process according to the invention for the production of powder coatings has the additional advantage that the fines, i.e. the powder 2147~79 _ coating particles having a particle size < 10 ~m, do not have to be separated off for the production of powder coatings having a small average particle size.
The powder coatings produced in accordance with the invention are suitable for coating a large number of substrates, for example metal, plastic, wood, glass and the like. They are preferably employed for coating metal components, in particular thin-walled metal components of large surface area, and above all car bodies.
The powder coatings are preferably applied by means of electrostatic assistance. Conventionally, the electrostatic charging of the powder coating particles is carried out by applying a high direct voltage in the vicinity of the powder discharge apertures at points or sharp edges on the spray gun. However, besides this it is also possible not to give the powder coating particles an electrostatic charge until after the spray nozzle.

Claims (20)

Patent claims:

1. Powder suspension, in particular powder coating suspension, characterized by a suspension of powder particles in a gas, in particular nitrogen, liquefied at a pressure of not more than 20 bar.

2. Powder suspension according to claim 1, characterized in that it contains components which are reactive at room temperature.

3. Powder coating suspension according to claim 1 or 2, characterized in that it contains a) binders containing active H atoms, in combination with compounds which contain free isocyanate groups or anhydride groups, b) compounds containing carboxyl or amino groups, in combination with compounds which contain epoxide groups or carbodiimide groups, c) compounds containing amino groups, in combination with compounds containing carbonate groups, d) systems which cure by the principle of Michael addition or e) moisture-curing systems.

4. Process for the preparation of a powder suspension according to one of claims 1 to 3, characterized in that a fine grinding of relatively coarse powder particles is carried out to an average particle size of not more than 15 µm, in particular 10 µm, by wet grinding, in particular in a stirred mill, the liquid medium for the wet grinding being a gas, in particular nitrogen, liquefied at a pressure of not more than 20 bar.

5. Process for the preparation of a powder suspension according to one of claims 1 to 3, characterized in that first of all the desired particle size of the powder is adjusted and subsequently the powder is suspended in a gas liqufied at a pressure of not more than 20 bar.

6. Process for the production of a powder coating on a substrate, wherein a suspension of powder particles, in particular powder coating particles, is sprayed and the spray jet is directed onto the substrate to be coated, characterized in that a powder suspension according to one of claims 1 to 3 is employed, and the liquid gas is vaporized before, during or after the spraying of the suspension.

7. Process according to claim 6, characterized in that the liquefied gas employed for the suspension of the powder particles has been liquefied under a pressure of not more than 10 bar, preferably at normal atmospheric pressure.

8. Process according to claim 6, characterized in that the suspension is heated indirectly prior to spraying at superatmospheric pressure.

9. Process according to claim 6, characterized in that the liquid gas drops are vaporized directly by radiant heating and/or by mixing the suspension with a heated stream of gas during spraying.

10. Process according to claim 9, characterized in that the suspension and the heated stream of gas are mixed in a two-fluid nozzle.

11. Process according to claim 9, characterized in that the suspension is sprayed in a two-fluid nozzle and the stream of gas has a temperature which is only slightly above the temperature of the suspension, and in that the liquid gas drops are vaporized by a second heated stream of gas.

12. Process according to claim 10 or 11, characterized in that the adjustment of the admission pressure of the suspension at the two-fluid nozzle is carried out by controlled heating or cooling of an insulated suspension supply vessel, from which the suspension is supplied to the two-fluid nozzle.

13. Process according to one of claims 6 to 12, characterized in that storage and transportation between the powder manufacturer and the processor is effected in insulated transportation vessels which contain the powder suspension which is used for the subsequent spraying and which comprises liquefied gas and powder particles.

14. Process according to claim 6, characterized in that the suspension of the powder particles in the liquefied gas is prepared in the actual nozzle and the liquid gas drops are vaporized a) indirectly and/or b) directly by radiant heating and, if desired, c) by mixing the suspension in the nozzle with a cooled stream of gas during spraying and/or d) by a heated stream of gas after spraying.

15. Process according to one of claims 6 to 14, characterized in that the powder particles have an average particle size of not more than 15 µm.

16. Process according to claim 15, characterized in that the powder particles have an average particle size of not more than 10 µm and a maximum particle size of not more than 20 µm.

17. Process according to one of claims 6 to 16, characterized in that the viscosity of the liquefied gas is < 5.10-4 Ns/m2, preferably < 10-4 Ns/m2.

18. Process according to one of claims 6 to 17, characterized in that the powder coating particles, electrostatically charged, are directed onto an earthed metal component.

19. Process according to one of claims 6 to 18, characterized in that it is employed for the production of catalysts.

20. Apparatus for carrying out the process according to one of claims 6 to 19, having a powder supply container or an insulated supply container which contains a powder suspension according to one of claims 1 to 3, a spray nozzle, a line which may be thermally insulated and which connects the supply container to the spray can [sic], and an apparatus for supplying the quantity of heat which is required for the vaporization of the liquid gas drops.