METHOD AND DEVICE FOR SPRAYING MIXTURES OBTAINED FROM THE REACTION OF POLYMER MATERIALS

Abstract

The invention relates to a method and a device for producing a thin article or a thin coating on a previously manufactured solid body. At least two reactive polymer materials (A, B) are mixed together thoroughly and die resultant mixture (M) is discharged via a nozzle (216) in the form of a thin tube (250). This thin tube is pulverized or atomized by means of the introduction of a controlled flow of pressurized air with the result that die pulverized mixture (Z) may be sprayed onto an open mould (300) or onto a surface (350) or onto a previously manufactured solid body which is to be coated.

Description

The present invention relates to a method and a device for spraying mixtures of reactive polymer materials, for example bi-component or multi-component polyurethanes, in order to obtain thin articles, i.e. articles with a small thickness, and to apply a thin coating onto previously manufactured solid bodies.

In the context of the present patent:

• • “spraying” refers to the use of pulverized (atomized) liquid mixtures;
  • the term “articles” is understood as meaning both finished products and components and semi-finished articles used to produce finished products;
  • “thin”, both in the case of articles and in the case of coatings, refers to a thickness which may be even less than one millimetre and in practice is between 0.1 and 4 mm;
  • “high definition” refers to the possibility of reproducing very fine designs or textures.

The conventional techniques for producing articles using basic components consisting of reactive polymer materials in the form of very viscous fluids as well as any auxiliary filler materials such as coloured pigments, flame retardants, etc., employ devices such as those described, for example, in the patent U.S. Pat. No. 3,035,775. In this device the basic components are thoroughly mixed together and pressurized air is added to the resultant reaction product (polymer mixture) so that it can be sprayed through an end nozzle.

These techniques are undoubtedly satisfactory, as demonstrated by their widespread use, but they have a number of important limitations with regard to the production of thin articles or coatings with very small and well-defined designs. In this case it is required to use spraying devices which ensure very small flowrates and which therefore have an end nozzle with a very small cross-section. A nozzle of this kind, however, becomes blocked very rapidly owing to the viscosity and reactivity of the basic components of the polymer mixture.

The device described in the patent U.S. Pat. No. 4,778,659 (corresponding to EP 0,209,888) comprises a splined shaft which is rotated at a speed of between 100 and 3200 rpm so as to receive sequentially and mix two reactive polymer liquids. The device comprises an outlet opening with substantially the same diameter as the shaft, through which the resultant reaction product, i.e. the polymer mixture, is discharged without being pulverized (atomized), and therefore this device is not a spraying device.

The main object of the present invention is to provide a method and a device for spraying mixtures of liquid polymer materials with a high viscosity and high reactivity so as to achieve the following results:

• • the articles thus obtained (the word “article” having the meaning as defined above) have mechanical properties such that they do not require in all cases a reinforcing substrate in order to be used;
  • both the articles and the coatings thus produced have a minimum thickness of less than 1 mm and a thickness on average of between 0.1 and 4 mm;
  • both the articles and the coatings may be high-definition, i.e. have a surface with very pronounced textures and with well-defined edges, allowing also very fine designs to be reproduced. This means that on the surface of articles and coatings it is possible to obtain clear writing which is legible by the naked eye even in the case of a minimum height of 5 American typographical points or Postscript, namely about 1.75 mm;
  • both the articles and the coatings are without the typical defects of articles produced with polyurethane mixtures, such as air pockets or cavities resulting therefrom.

The invention is able to achieve this object and other objects by imparting to the reaction product (polymer mixture with at least two basic components) a tube-like form with a thickness of less than 1 millimetre and pulverizing or atomizing this tube the instant it emerges from the device inside which the basic components are thoroughly mixed together.

These characteristic features and the associated advantages will emerge more clearly from the following description of a non-exclusive embodiment of the present invention, with reference to the accompanying drawings, in which:

FIG. 1 shows a three-dimensional and partly sectioned view of a device according to the invention for spraying polyurethane obtained by mixing basic components consisting of polyol and isocyanate (with any required additives);

FIG. 2 shows a variant of the device according to FIG. 1;

FIGS. 3 and 4 show, on a larger scale, the two configurations (open configuration and closed configuration, respectively) of one of the valves by means of which the abovementioned basic components are supplied to the device;

FIG. 5 shows in schematic form, with certain details enlarged, how the aforementioned basic components are mixed inside the device, resulting in a tube-like form of the mixture produced;

FIG. 6 shows an enlarged view of the part of the device where pressurized air is blown onto the mixture;

FIG. 7 shows how, in the same zone shown in FIG. 6, the mixture is imparted a tube-like form at the moment when it is pulverized (atomized) and therefore sprayed by the pressurized air;

FIGS. 8, 9, 10A and 10B show different modes of use of the present invention.

With particular reference to FIG. 1, the device according to the invention comprises in a manner known per se an elongated casing 210 which encloses a first cylindrical chamber 212 and, in succession along the same axis X, a second frustoconical chamber 214 which terminates in a spraying nozzle 216. A helical-profile screw 218 operates inside the chambers 212 and 214 and is able to rotate about its axis at a variable, but very high speed, ranging between 8000 and 30,000 rpm, so as to mix the reactive components and to move in both directions along the same axis until it emerges partially from the nozzle so as to clean it of any remains of the resultant mixture. The end part of the screw 218 has in fact a diameter which decreases, like the second chamber 214 of the casing 210, to a minimum value equal to the value of the diameter of the nozzle 216. For operation of the screw 218, the device comprises, respectively, also an electric motor 220 and a cylinder unit 222.

The variant shown in FIG. 2 differs from the device according to FIG. 1 only in that the elongated housing 211 encloses a single cylindrical chamber 215 inside which a mixing screw 219, which is also cylindrical, operates. The other parts of this device are the same as those shown in FIG. 1 and therefore retain the same reference numbers.

As mentioned hereinabove, up to this point in the description, the device is conventional, while the characteristic features described from this point onwards are regarded as novel and original, at least in terms of their combination, in that as a result it is possible to achieve results, described more fully below, which cannot be achieved by the state of the art.

A first characteristic feature of the present invention, illustrated by the enlarged views in FIGS. 3 and 4, is that the along the whole length of the mixing screw 218 the clearance between the crest of its helical profile and the surface 213 of the chambers 212 and 214 is constant and has a value of less than 1 millimetre, and preferably a value of between 0.08 and 0.3 millimetres. The same clearance also exists between the mixing screw 219 and the surface 217 of the chamber 215 in the variant of the invention shown in FIG. 2.

A second characteristic feature relates to the two one-way metering valves 224 and 226. The valves receive the basic components in the liquid state (A=polyol and B=isocyanate when the mixture M is polyurethane) via inlet channels 225 and 227 which communicate with respective storage tanks (not shown) and introduce these basic components into the first chamber 212 via respective radial supply channels or openings 221 and 223 which are arranged on the surface 213 of the chamber 212. The metering valves 224 and 226 are proper injectors comprising injection needles 231, 233 which interact with the supply openings 221 and 223 and are operated in an adjustable manner by respective solenoids 235, 237 or other conventional means so as to obtain very low values, ranging between 0.05 and 8 grammes per second of the resultant mixture.

A third characteristic feature, already mentioned hereinabove, is that the end diameter, i.e. in front of the nozzle 216 of the mixing screw 218 (or, respectively, the sole diameter of the screw 219) is the same as the diameter of the said nozzle 216 and ranges between 6 and 15 millimetres—see FIG. 6.

A fourth characteristic feature, which is illustrated in the enlarged view of FIG. 6, consists in the configuration of the end part of the device according to the present invention, i.e. the mixture is pulverized (atomized) with the local introduction of pressurized air so as to be sprayed. The pressurized air reaches, in fact, via a plurality of openings 244 (as indicated by the arrows L), a ring 240 which surrounds the end part of the elongated casing 210 (or 211, respectively) with a calibrated radial clearance 242 and has a head 246 with a front clearance 245 which is also calibrated. The position of the ring 240 is adjustable along the axis of rotation X of the mixing screw 218 (or 219, respectively) so as to vary the pressure of the air which emerges from the front clearance 245 of the ring 240 exactly at the end of the nozzle 216.

As a result of the characteristics features described above, in a device according to the invention, the very small clearance between mixing screw 218 and inner surface 213 of the corresponding chamber 212 inside the elongated casing 210 produces laminar flows of the basic components A and B which are gradually mixed and react producing the mixture M. In the chamber zone closest to the nozzle 216 the mixture therefore assumes the form of a very thin tube 250, i.e. with a thickness not greater than 1 millimetre and a diameter substantially the same as the end (or sole) diameter of the mixing screw 218 (219)—see in particular the enlarged details of FIG. 5. In this way the flowrate of the mixture discharged via the nozzle 216 has very small values (between 0.05 and 8 grammes per second) already mentioned hereinabove.

This tube 250 is pulverized or atomized by the pressurized air which emerges from the front clearance 245 of the ring 240 and the mixture M may therefore be sprayed, as indicated schematically by the fan-like form Z in FIG. 7. The amplitude or “range” of the sprayed mixture M, indicated by the arrows S in the same FIG. 7, may be varied by adjusting the pressure of the air which emerges from the front clearance 245 of the ring 240.

FIGS. 8, 9, 10A and 10B show different ways of spraying the mixture. These figures show, in an entirely schematic form, a device according to the present invention, indicated by D, and the fan-like spray Z of the mixture M produced by it.

As a result of the invention, in fact, it is possible to obtain an article with a minimum thickness of 0.1 millimetre, reproducing a design with a very fine texture:

• • both when this design is present on an open three-dimensional mould 300 (for example that of a shoe sole, see FIG. 8);
  • and when the design is present on a flat surface 350, so as to obtain a “printed” sheet F (see FIG. 9 which, in the right-hand drawing, illustrates the moment when it is detached from the surface 350, schematically represented by the hands H. In this case, during spraying, a relative movement may be required, schematically indicated by the arrows Y1 and Y2, of the device D and the surface 350 in order for the latter to be fully and uniformly covered);
  • or in order to obtain a coating, also with a minimum thickness of 0.1 millimetres, of a three-dimensional body manufactured previously, for example a chair 410, see FIG. 10A (in this case also a relative movement of the device D and the chair 400, schematically indicated by the arrows Y1 and Y2, may be required) or a sports shoe—see FIG. 10B.

A further characteristic feature of a device according to the invention consists in the use of a helical profile of the mixing screw 218 (or screw 219, respectively) of the multiple-thread type. A profile of this type has two or more valleys (not shown) which are parallel and arranged symmetrically with respect to the axis of rotation of the screw so as not affect the dynamic balance of the said screw. This fifth characteristic feature, however, is not indispensable for achieving the desired results, in contrast to the four characteristic features previously described.

From the above description it can be understood that the abovementioned objects are achieved and that the nozzle becomes blocked very rarely, if at all, since its diameter is the same as the diameter of the mixing screw or at least its end part.

Within the scope of the following claims, the method and the device according to the present invention may also be realized in ways different from those described hereinabove.

Claims

1. Method for producing a thin article or a thin coating on a previously manufactured solid body, comprising the steps of: introducing at least two basic components (A, B) of reactive polymer materials in a fluid state into at least one chamber (212, 214; 215) provided inside a casing (210; 211) having a nozzle (216) at one end;obtaining a mixture (M) from the reaction of said basic components by means of a helical screw (218; 219) which is able to rotate about its axis (X) and to move linearly along it inside said casing (210; 211);discharging the mixture (M) through the nozzle (216),characterized in thatin the zone of said chamber which is closer to the nozzle the mixture (M) is imparted the form of a thin tube (250);a controlled flow of pressurized air is introduced at the end of the nozzle (216) to obtain a pulverization or atomisation of said thin tube with the result that the mixture (M) can be sprayed;the pulverized mixture (Z) is sprayed onto an open mould (300) or a surface (350) or said solid body (400).

2. Spraying device comprising: a casing (210; 211) enclosing at least one chamber (212, 214; 215) having a nozzle (216) at one end,radial openings or channels (221, 223) for feeding reactive basic components (A, B) in a fluid state of a polymer mixture (M), said openings or channels being provided on the surface (213) of one chamber or of the chamber (212; 215), whereby the said basic components may contain additives depending on the application or use of the mixture,a mixing screw (218; 219) with a helical profile extending along the axis (X) of said at least one chamber,means (220, 222) for operating the mixing screw so as to cause it to rotate about said axis (X) and move linearly along it,characterized in thatthe end diameter of the mixing screw (218) in front of the nozzle (216) is the same as the diameter of the nozzle itself,a ring (240) comprising a free head (246) encircles with a calibrated radial clearance (242) the end portion of the casing (210, 211) and has a position adjustable along the axis of rotation (X) of the mixing screw (218; 219), the said ring being provided with openings (244) for introducing pressurized air onto the mixture (M) discharged by the nozzle (216) through a front clearance (245), also calibrated, so as to pulverize or atomize the mixture so that it can be sprayed.

3. Device according to claim 2, characterized by the combination of the following features: a constant clearance of less than 1 millimetre is provided between the surface (213) of the at least one chamber (212, 214; 215) of the casing (210; 211) and the crest of the helical profile of the mixing screw (218; 219);the rotational speed of the screw during mixing of the basic components is at least 8000 revolutions per minute;the end diameter of the mixing screw (218) in front of the nozzle (216) is between 6 and 15 millimetres.

4. Device according to claim 3, characterized in that the rotational speed of the screw during mixing of the basic components does not exceed 30,000 revolutions per minute.

5. Device according to claim 3, characterized in that the clearance between the surface (213) of the at least one chamber (212, 214; 215) of the casing (210; 211) and the crest of the helical profile of the mixing screw (218; 219) is between 0.08 and 0.3 millimetres.

6. Device according to claim 3, characterized in that the helical profile of the mixing screw (218; 219) is of the multi-thread type with two or more parallel valleys which are arranged symmetrically with respect to the axis of rotation (X).