GB2121350A - Composite foamed articles and process for their production - Google Patents

Abstract

Process for making composite foamed articles by impregnating an open-celled organic foam with an aqueous suspension of an insoluble solid impregnant to deposit the solid within the pores and then drying, using a closed mould system in which the foamed article is confined so that it seals with the walls of the mould and allows differential pressures to be built up across the thickness of the foam. These are used to assist impregnation, control degree of penetration of the impregnant, and drawing off excess liquid. Useful for making fire-resistant tiles from partly expanded polystyrene beads and can include surface-finishing and other steps. In one embodiment, a foam block (4) is moulded in a cavity defined by mould parts (1) and (2), the parts moved slightly apart, impregnating material (5) introduced into the space between the parts, and the parts reclosed to force the impregnating material partially or fully into the block. In another embodiment a second mould, not that used for forming the block, is used to effect impregnation. The second mould may or may not further shape the block. <IMAGE>

Description

SPECIFICATION Composite foamed articles and process for their production This invention relates to composite foamed articles and to an improved method for making them.

It is well known to make foamed articles from foamable organic materials by confining a foamable material in a mould and then applying heat so as to bring about foam formation. This is usually done by using a mixture of the polymeric organic material to be foamed (or of the chemical precursors from which it is made) and a foaming or blowing agent which is activated by heat to bring about the desired foam formation. If desired, pre-expanded beads of foamed polymer may be injected into a mould and then further expanded within the mould by the action of heat.The procedure may be carried out using a mould comprising a single pair of mating components for the mould and applying all the necessary heating and cooling cycle for the production of the final shaped article to this (the "standard mould" process) or by using two sets of mating mould components, one hot and one cold, and transferring the partly foamed material from the hot mould set to the cold mould set during the course of the foaming, shaping and cooling sequence (the "transfer mould" process).

in the case of foamed articles in which the foamed material is produced by a chemical reaction, the components required may be mixed and injected into a mould (open or closed) in which the foam formation takes place. The foam formation may be assisted by the presence of components which function as a foaming or blowing agent in consequence of the heat of the chemical reaction. In such cases, heating or cooling may be applied to the mould, and in general a "standard mould" process is conveniently used.

Such processes have the advantage of being easily operated, but in some instances the foamable materials can be highly combustible and dangerously inflammable. It is therefore highly desirable that there should be an efficient and satisfactory method available for the production of composite foamed products which can have substantially safer properties, using the existing moulding techniques and equipment without detriment to their ease of operation and production and with minimum need for modification.

It is known that a wide variety of additives, and especially particulate inorganic additives, can be incorporated in organic polymer compositions to modify their properties. A difficulty usually encountered with their use, however, is that of incorporating them satisfactorily and in an adequately controlled manner without interfering with the foam formation or having to introduce troublesome or expensive variations to the commonly used and established methods and apparatus of the industry.

Many attempts to incorporate an additive into foamed materials by impregnation at a stage after foam formation can fail, or achieve only an unsatisfactory degree of impregnation, even when pressure or vacuum are used to assist the treatment. This may be due to the foamed material having a closed pore structure which effectively prevents entry of the impregnant, or to uncontrolled access of the impregnant which results in incomplete or uneven impregnation.

I have now found that improved incorporation of additives so as to form an improved composite foamed material can be achieved by a procedure using moulds.

Thus according to my invention I provide a process for making composite foamed articles which comprises taking a foamed organic material at a stage at which it has an open-celled porous structure, confining it in a mould so that there is substantially sealing contact with the mould around its periphery ("a peripheral seal") and so that there is a gap between the mould wall and the foamed material at a face of the foamed material on one side of the peripheral seal, injecting an aqueous suspension of the desired impregnant material into the said gap, then forcing the said suspension into the open pores of the foamed material by application of an appropriate pressure difference across the peripheral seal, and then removing the impregnated foamed material from the mould and drying it.

My invention is especially applicable to the production of articles which are relatively thin, in relation to their overall size, and most of all to articles which are given a decorative, textured or otherwise selected final finish from contact with the mould. An example of such a product is a decorative tile (for example a ceiling tile) but the invention is in no way limited to such specific articles.

The procedure of my invention can be carried out in a variety of ways. Firstly, foamed material with the open-celled porous structure may be produced in situ in the mould or it may be made separately and transferred to the mould for subjection to treatment according to the process of the present invention. If it is produced in situ this has the advantage of simplifying the overall procedure, but care has to be taken to ensure that the desired open-celled structure is produced; this is a matter usually settled easily by the experience and skill of the operator or by the established results known to be achieved by the process conditions used for the initial foam formation. If the foamed material is made separately, for example in a block or sheet form, a piece to fit the mould may be cut from the block or sheet and transferred to the mould.

I find that it is generally desirable for the foamed material of open-celled structure to fit the closed mould well (especially, but not only, at the periphery) so that the impregnation can take place in a controlled fashion and direction from a selected face of the article. Otherwise, it can be more difficult to regulate the impregnation if the ingress of the impregnant can take place from several directions or if the rate of impregnation can vary because of uncertain or irregular spaces between the mould and the foamed material within it. Consequently, it is very convenient to form the foamed material, with its desired opencell structure, in situ within the mould as this generally simplifies procedure and keeps down the number of operations.If this procedure produces a product which has the desired open-cell structure throughout the body of the material but has a surface skin which is relatively impermeable, it may be convenient to open the mould and remove this skin or surface layer (for example with a knife blade or other convenient cutting or slicing device) to expose the open-cell structure beneath before proceeding to the impregnation step.When the foamed material to be impregnated has been made separately, it is particularly desirable to ensure that it fits the mould well, and this can be done by subjecting it, within the mould, to heat or pressure or such combination of these as will stabilise the foamed material within the mould and cause it to move (whether by expansion, contraction, relaxation, softening or whatever reason) sufficiently to fill the mould well and close up any undesirable spaces between the foamed material and the mould walls, and especially to form the peripheral seal.

When it has been established that the foamed material adequately fills the mould and the peripheral seal has been achieved, the gap between the mould wall and the foamed material which is required for the next step of the process of my invention may be formed by partial separation of the components of the mould. This operation is termed "backing off" the mould. The space formed in the mould can be determined with good accuracy by measurement or by predetermined setting of the extent of separation of the mould components.

The injection of the aqueous suspension of the desired impregnant material into this gap may then be carried out through suitable holes or channels serving as inlets into the mould system (i.e. in one or both of the mating components of the mould). This may be done in conventional manner, by preparing the suspension and then injecting it by pressure using suitable measuring devices, non-return valves and the like to ensure the delivery of the desired amount of the suspension and the avoidance of any premature settling-out of the impregnant from the suspension.The quantity of the suspension used should normally be sufficient to fill substantially completely the gap within the mould, and the gap itself should normally be such as to be equivalent in volume to the total accessible voidage (i.e. the total volume of all the open cells within the foamed material which it is intended to fill with the suspension). Lesser amounts of suspension, insufficient to fill the gap, will tend to leave part of the receptive surface uncovered or unimpregnated, and this is best avoided unless for some reason an uneven distribution of the impregnant is actually desired. If incomplete impregnation of the foamed material is desired, for example impregnation only to a selected depth, then adjustment of the gap within the mould may be made so that it corresponds to the appropriate fraction of the total open-cell voidage of the foamed material.The formation of the suspension and its injection into the gap should, for preference, avoid appreciable aeration of the suspension as the presence of air bubbles may cause undesirable separation of the suspension and consequent uneven impregnation.

The forcing of the impregnating suspension into the open-cell pores of the foamed material may be achieved in a variety of ways. The pressure difference necessary to achieve it may be secured simply by closing the inlet (feed lines) for the impregnant suspension and then moving the mating components of the mould together so as to diminish the internal gap which now contains the impregnant suspension and thereby force the impregnant suspension into the open cells of the foamed material. This alone may be rather inefficient if the opposite side of the mould, remote from the impregnant suspension, is sealed because a back pressure will tend to build up and progressively impede the flow of the impregnant suspension as the mould components move towards each other, and the impregnant may tend to concentrate at the face of the foamed material at which it enters.More even impregnation throughout the mass of the foamed material may be achieved by providing drainage channels or outlets in the mould component on the remote side which can be opened to allow air and/or water and/or surplus suspension to escape as the closing of the mould components forces these through the foamed material. Advantageously, the differential pressure across the foamed material may be increased, and the rate of flow of the impregnant suspension into the foamed material may be correspondingly increased by applying suction or vacuum to these drainage channels or outlets.

Usually, such suction or vacuum need not be applied after the foamed material has been fully impregnated, as evidenced by the emergence of surplus suspension through the outlet channels.

The resulting impregnated foamed material is thus effectively charged, to the extent of all or part of the open-cell voidage of the foamed material, with water and the impregnant, and may be removed from the mould and dried to remove the water and leave a dry composite impregnated article. Such drying, which may be aided by heat or other conventional means, may often be inconveniently slow, so I prefer to assist the drying operation by one or more optional steps. In particular, the suction applied to the outlet channels of the mould may be continued, provided that this does not appear to be removing undue amounts of the impregnant and thereby depleting the desired degree of impregnation. If the foamed material is resilient, then some of the water content can be expelled by compression of the foamed material.This compression can be taken to whatever degree is acceptable; for example it may be taken far enough to expel appreciable amounts of the water without expelling appreciable amounts of the impregnant, or it may be taken only to such a degree of compression that the limits of resilience are not exceeded and the foamed material does not remain undesirably deformed when the compressive forces are released. It is, of course, possible that some deformation may be acceptable or even desirable as part of the shaping process for the final product, and in such cases it is quite acceptable to compress the foamed. material beyond its recovery limits so that, for example, a surface pattern or finish can be effectively embossed thereon.

Final drying of the impregnated foamed material may be carried out by conventional means, for example by heating it in an oven or in a stream of hot air, by dielectric heating, or by any other means or combination of means-for promoting evaporation or removal of the water until a satisfactorily low level of residual water results.

The foamed organic materials which may be treated by the process of my invention may be of any kind provided that they have the requisite open-cell structure. Thus they may have resilient (flexible) or non-resilient (rigid or. semi-rigid) properties, and may be thermoplastic or thermosetting in their mode of formation, or any combination thereof.

As many methods for making foamed organic products (for example foamed thermoplastics, and notably foamed polystyrene) give products having a closed-cell structure, care must be taken to secure an open-cell structure or its equivalent if my process is to be used for its treatment. For the purposes of my present invention, the definition of the foamed material as having "an open-cell structure" includes materials made from a foamed material having a basically closed-cell structure but also a multiplicity of inter-communicating interstitial gaps and spaces within it which can behave as the equivalent of an open-cell structured foam and be impregnated by the process of the present invention.Examples of such materials included for this reason may be made by taking pre-foamed beads or fragments of a polymer (for example foamed polystyrene) and adhesively bonding them together so that, although they adhere to each other sufficiently to form a mass of some reasonable strength, the beads or fragments are not pressed completely together and residual interstitial gaps and spaces are left which intercommunicate sufficiently to give the mass a permeability similar to that of a true open-cell structure. These materials may be made by a controlled compression of foamed polymer beads under the influence of heat (which softens them and makes them stick to each other) or of some other added adhesive, usually in a mould, whereby the material is converted into a porous form which becomes stabilised when the material is cooled back to ambient temperature or the adhesive has set.

My process may also be applied with especial advantage to resilient foamed materials, for example cellular rubbers or foamed thermoset polymeric materials, for example polyurethanes, and the like. In these cases the procedure is essentially as described above but additional beneficial results may be obtained. Thus in particular the impregnation may result in imparting not only the properties inherent in the impregnant used but also a useful modification of the resilience or flexibility of the resilient foamed material. The impregnant can change the resilience to any desired extent (usually, but not necessarily, by making it stiffer or less resilient).

This effect may be brought about substantially uniformly throughout the material, or selectively or progressively through it, or even concentrated selectively in localised areas for example at the article's surface. This enables my invention to be used by a manufacturer to produce a material in which the core portion retains its own normal mechanical and physical properties (for example flexibility) substantially undiminished while the surface or surface zones can be given modified properties, for example improved stiffness, wearresistance or fire-resistance.

These variable effects may be achieved by appropriate choice of impregnants, proportions of impregnants, and the methods of impregnation, as more fully described hereafter. In the extreme, my invention can be used to transform a resilient foamed material into a rigid or semi-rigid one.

The procedure may also be applied to a wide variety of other foamed organic materials and not only to those mentioned above, belonging to many chemical constitutions. For example they may be polyurethanes, polyesters, phenolic resins (e.g.

phenol-formaldehyde resins), polyolefines (for example polyethylene, polypropylene), polyimides, polyvinyl chloride, polyvinyl carbazole, urea- formaldehyde products, acrylic polymers, and mixtures and combinations thereof.

The particulate inorganic material may be any one or more materials which are substantially insoluble in water, stable (for example thermally and hydrolytically) at ambient temperatures and temperatures at which the impregnated composite foamed material is to be used.

Preferably, the inorganic material should be able to impart some desirable property to the foamed material though it may be an inert material added for purposes such as loading or "densifying" the foamed material. Especially useful impregnants are those which have a retarding or inhibiting effect on the melting, burning and/or vapourisation phenomena which so commonly occur when foamed materials are heated or ignited, and are a source of danger in their industrial use. Examples of suitable inorganic impregnant materials include carbonates, phosphates, silicates, fluorides and other salts of metals such as calcium, magnesium, aluminium and the like, metal oxides (for example silica, alumina, alumina tri-hydrate), cements, calcium sulphate, and mixtures and combinations thereof.I especially prefer that the impregnant is a layer mineral, for example a vermiculite, clay (e.g. ball clay, china clay, fireclay), montmorilionite/ bentonite, kaolinite, sepiolite and mixtures thereof. These materials may be used if so desired in any processed or un-processed form, ranging between the natural materials (subjected to any desired grading, grinding, purification or separation procedures needed to bring them into a state of appropriate usefulness) to forms which have been made by modification of the natural structures (for example by heat or by chemical treatments) to render them more useful.

I especially prefer to use a layer mineral (especially a vermiculite) which has been chemically delaminated into extremely small, thin, plate-like particles known as lamellae. Methods for the preparation of these are well known in the art and are described for example in German Offenlegungschrift No. 2741859, in United Kingdom patent specifications Nos. 1016385, 1076786,1119305 and 1585104, and by Baumeister and Hahn in "Micron" Vol. 7, page 247 (1946). Minerals, for example montmorillonites, which have been subjected to ion-exchange treatments (for example to replace calcium ions by alkali metal ions, for example sodium ions) may also be used.

The particle size of the inorganic impregnant may vary considerably, but preferably should be smaller by orders of magnitude (e.g. one twentieth or even smaller) than the size of the cells of the foamed material, so that the particles can penetrate easily and well into the interior of the foamed material. A very suitable size for the particles is in the range 50 to 100 microns, and desirably the particles should be of a shape having a high aspect ratio. In the case of delaminated layer minerals, for example vermiculite, the use of lamellae as small as practicable is preferred, even smaller than the 50 to 100 microns indicated above, and having high aspect ratios which may be over 100:1 or even over 1000:1.

The aqueous suspension of the inorganic impregnant may be made in conventional fashion.

The suspension may contain surfactants, dispersing agents and other conventional additives to disperse the particles and/or to inhibit flocculation or breakdown of the suspension; such additives may be cationic, anionic or non-ionic in nature, and matched appropriately to the particles to be suspended and to the foamed material to be impregnated.The proportion of the solid particles of impregnant in the aqueous suspension may vary considerably; usually the main requirement is that the suspension should carry enough suspended solid to enable the desired amount to solid to be carried into the cells of the porous material and deposited there with a minimum difficulty and the minimum amount of water (which needs to be removed later), balanced with the suspension itself having a thickness or viscosity which is not so high as to make the penetration of the suspension into the foamed material unduly slow, difficult or uneven.

Convenient proportions may range widely, for example from 10% to 50% by weight of solids particles in the aqueous suspension used. In some cases, high proportions of solid can be used if the I suspension is still suitably fluid for use in the impregnation.

As indicated above, the extent of penetration of the impregnant into the open-cell structure may be through substantially the entire matrix of the foamed material, but when the fire protection or other effect provided by the impregnant is adequately achieved by a surface coating and/or limited penetration (for example to several cellular layers below the surface) this can be done by controlling the quantity of impregnant and the method of impregnation. The important feature, however, is that the solid impregnant should not lie entirely upon the surface as a surface coating but sufficient penetration into at least the outermost layers of cells of the foamed material should take place in order to provide a good anchor for the impregnant.

I find it advantageous that my process can be used to achieve graded or differential impregnation effects by using successive suspensions of different impregnants, so that one impregnant may become located in the core region of the foamed material (by injecting that one first) and another one may be predominantly located at or nearer to the surface zones (by injecting that one later). As an alternative to the technique of successive injections, some differentiation of the impregnation in different zones of the foamed material can be achieved by varying the size distribution of the impregnant particles so that some can penetrate deeply while others, being larger, cannot penetrate so far and consequently tend to concentrate at or near the surface.

As a further feature of my invention to improve the products I also find it advantageous to provide a sufficient excess of the impregnant, above that required for the selected interstitial penetration, to provide a surface layer of concentrated particles of the impregnant material.

This may serve as a further modification of the structure of the surface or even to provide a coating intended for more decorative or protective purposes. This may be done by making the main impregnation charge of suspension slightly less than that required to fill the voidage or interstitial volume of the matrix, assert the pressure differential so as to force the suspension into the matrix of the foamed material, and then inject a further charge of suspension (which need not be the same as the first suspension) into a gap made by "backing off" the mould components again, and then repeating the pressure differential stage so as to force the second suspension into the surface of the foamed material. By using an amount greater than is necessary to fill the remaining pores, the excess which does not penentrate will form a surface layer of slurry which, on drying, will become a surface coating on the face of the product held there by the "keying" effect of the partial penetration and of the partial commingling of the different impregnant layers.

The impregnant material may be organic in nature if desired, and mixtures of different impregnants (inorganic and organic) may be used if so desired. Examples of organic impregnants include natural and/or synthetic organic polymers in the form of latices or dispersions in aqueous media, having particle sizes substantially as indicated above for inorganic impregnants.

Particular examples include polyvinyl chloride, acrylic, and polyolefine (for example polyisoprene) aqueous dispersions. These organic impregnants may be substantially stable polymers or curable polymers which may be "cured" (i.e. undergo further chemical reaction) under the influence of heat or other conventional agents, to achieve further modification of the bonding of the impregnant and/or the foamed material.

If the suspensions of impregnants used in the process of my invention contain components which, though necessary for the formation and/or use of the impregnant suspension, are not desirable in the final composite impregnated foamed material (for example water-soluble materials, surfactants, colloids and the like) it may be desirable to carry out a final operation to remove them after the impregnant has been put in place. This may be done by careful washing with water, taking care that the washing operation does not also remove an undue amount of the impregnant. Washing may be carried out by feeding a suitably slow flow of water (usually unheated) into the inlet (feed) side of the mould system described above so that it runs through the pores of the foamed material and out through the outlet side of the mould system.Alternatively, the wash water may be kept on the inlet (feed) side of the mould system and used to wash away any aqueous solution or suspension which has not impregnated the foamed material or formed a suitable sedimentary coating on its surface. Such purging or cleaning may also need to be applied to the mould system itself, and possibly a drying operation also, if the presence of water, residual surfactants and the like from some stages of the process tend to interfere with satisfactory operation of the later stages.

When the foamed material has been impregnated and dried as described above, it may with advantage be given a final treatment so as to modify or enhance it still further. For example, it may be subjected to heat (especially within a mould) to harden the surface, integrate the impregnant and/or surface layer more closely with the foamed material (for example by partial fusion or by some form of physical or chemical bonding) or to complete the foaming process or modify the cellular structure of the foamed material if this has not already achieved its final form. In particular, such treatment may impart to the product the final aesthetic appearance desired for sale of the product.

Similarly, the article may be given an aftertreatment to modify its properties still further or to adapt it for sale or use for particular purposes. This may be for example an after-coating treatment intended to colour, decorate or waterproof it, or to apply an adhesive coating or a protective coating (for example a detachable paper or plastic film coating) or any combination of these. The aftertreatment may even be a physical treatment intended to improve the article's shape, texture or other properties.

The invention is illustrated but not limited by the accompanying drawings, which are not to scale but represent schematically the operations carried out to produce a foamed composite ceiling tile.

In Figure 1 , the six illustrations labelled Fig. IA to Fig. 1 F represent the conventional "standard mould" process, adapted for the purposes of the present invention. The numerals used to indicate parts have the same meaning in all Figures 1A to 1 F.

The mould system comprises the two mould components - the male component (1) and the female component (2). Through an inlet channel (3) are fed the foamable polystyrene beads which are to be converted into the desired tile, so that they lie in the space between mould members (1) and (2). Heat is then applied (by means not shown, but conventionally by steam heating) to one or both of the mould components (1) and (2) so that the enclosed polystyrene beads foam and turn into a foamed body (4). Cooling means (not shown, but conventionally a cold water supply) are then applied to mould component (1) and, if desired, to mould component (2) to cool and stabilise the foamed body (4) within. The foamed body (4) is effectively the partly-made ceiling tile.This heating step must be carried out using temperature, time and other relevant conditions to give a foamed product (4) having the high degree of interstitial porosity necessary for impregnation.

(See Fig. 1 A and Fig. 1 B.) The next step is to retract male component (1) to an extent necessary to leave a space between its inner face and the surface of the contained foamed body (4). Into this space (5) is injected the requisite amount of impregnant suspension (for example an aqueous suspension of vermiculite particles) to fill the space (5) substantially completely. (See Fig. 1 C.) Then suction is applied through channels (not shown) suitably placed in the female mould component (2) in the region remote from the space filled with the aqueous suspension (5), and the suspension is drawn into the cells of the foamed body (4). This operation is usually carried out so as to fill substantially all the open cells of foamed body (4) but can if desired be adjusted to fill only a fraction of them.Any surplus suspension which does not fully penetrate into the depths of foamed body (4) will form a surface layer of concentrated impregnant particles on the surface of the foamed body (4) or a highly concentrated impregnation layer on the surface at which the suspension enters (6). (See Figure 1 D.) The mould components (1) and (2) are then closed together, and pressure applied to force them together sufficiently to consolidate the composite mass of impregnant and foamed body.

This can be done cold, or with the application of heat, as desired, to modify the structure of the foamed body (4) for example to achieve further foaming and cell modification, or to improve the surface finish and/or design on the on the foamed body's surface. Further suction may be applied if desired to remove some of the contained water of the injected suspension. (See Figure 1 E.) Finally, the composite impregnated foamed article (see Figure 1 F), in this particular instance the ceiling tile, may then be removed from the mould by conventional means, and a composite article comprising the impregnated foamed body (4) and optionally the surface layer (6) results. This can then be dried by convenient means (for example in an oven) not shown.

In Figure 2, the eight illustrations labelled Fig.

2A to Fig. 2H, represent the conventional transfer mould process adapted for the purposes of the present invention.

The mould system comprises the two mould components - the male mould component (1) and the female mould component (2)~with a foamed body (3) formed in the space between them in conventional manner, as described more fully above for Figure 1. (See Figure 2A.) The hot female component (2) with the contained hot foamed body (3) is then transferred away from the hot male mould component (1) to corresponding cold male mould component (4).

The foamed body is then transferred to the cold male mould component (4), the hot female mould component (2) is then returned to the hot male mould component (1) so that recharging with foamable polystyrene beads and foaming in the mould can be repeated. At the same stage a facsimile female mould component cold, (6) is brought together with the cold male mould component (4) and the contained foamed body (3), and the two mould components closed together to stabilise the foamed body by appropriate cooling. (See Figures 2B, 2C, 2D and 2E.) The procedure with the foamed body (3) now enclosed between cold mould components is continued as described above with reference to Figures 1 C to 1 F. (See Figures 2D to 2F.) The male mould component (4) is retracted ("backed off") to the extent necessary to leave a space between it and the contained foamed body (3), and into this space (7) is injected the requisite amount of impregnant suspension (for example an aqueous suspension of vermiculite particles) to fill the space substantially completely. The suspension is then forced, by suction applied from the female mould section at the back of the foamed body (3) to draw the particles of impregnant into the pores of the foamed body, optionally also forming a surface layer or higher level concentration at or near the surface in a zone (8) in the manner more fully described for the process illustrated by Figure 1. The mould components (4) and (6) may be closed together, with or without the application of heat, and dried by convenient conventional means.The pair of mould components is then ready for re-use with the next formed foamed mass from moulds (1) and (2).

The product is found to be a very satisfactory decorative ceiling tile, which can be affixed in place by conventional means. The impregnation with solid impregnant (in this particular example, vermiculite) imparts to the product the properties of fire-resistance, density and the like inherent from the characteristics the impregnant is known to give. In addition, the procedure described above enables conventional moulding lines and moulding machinery to be used with no appreciable or expensive modification to produce impregnated composite tiles. The "transfer moulding technique has the known advantage of saving both energy and time in the heating and cooling cycles of moulding, and can be used with continued advantage and minimal disturbance.

Finally, the procedure of the present invention enables the formation, impregnation and surface finishing of the tile product to be achieved in a well integrated fashion with little or no disturbance or conventional procedures already established for currently producing nonimpregnated products. This greatly enhances the ease of securing the valuable advantages of impregnants in foamed plastic tiles in particular.

It should be appreciated that, while this description above relates in detail to selected or specified materials and to formation of foamed tiles, the invention is not so limited and may be applied far more extensively, as is discussed more fully above.

Throughout this description, the moulds are illustrated as being vertically disposed. This not essential, but is the conventional way in which commercial moulding machinery is often operated.

For my invention, this disposition does not adversely affect operation as the steps are usually sufficiently speedy that the suspension of impregnant has little or no opportunity to settle out. However, if desired, the moulds may be used at any angle, ranging between the extremes of horizontal and vertical, as the operator desires and the actual disposition chosen appears in most cases to have little effect on the results obtained.

Claims (28)

1. A process for making composite foamed articles which comprises taking a foamed organic material at a stage at which it has an open-celled porous structure, confining it in a mould so that there is substantially sealing contact with the mould around its periphery ("a periphery seal") and so that there is a gap between the mould wall and the foamed material at a face of the foamed material on one side of the peripheral seal, injecting an aqueous suspension of the desired impregnant material into the said gap, then forcing the said suspension into the open pores of the foamed material by application of an appropriate pressure difference across the peripheral seal, and then removing the impregnated foamed material from the mould and drying it.

2. A process as claimed in Claim 1 wherein the foamed organic material with the open-celled porous. structure is produced in situ in the mould.

3. Process as claimed in Claim 1 wherein the foamed organic material with the ppen-celled porous structure is made separately and transferred to the mould for impregnation.

4. Process as claimed in any of claims 1 to 3 wherein the material is subjected, within the mould, to heat or pressure or such combination of these as will stabilise the foamed material within the mould and cause it to move sufficiently to fill the mould well and close up any undesirable spaces between the foamed material and the mould walls, and especially to form the peripheral seal.

5. Process as claimed in any of Claims 1 to 4 wherein, when it has been established that the foamed material adequately fills the mould and the peripheral seal has been achieved, the gap between the mould wall and the foamed material which is required for the next step of the process of my invention may be formed by partial separation of the components of the mould.

6. Process as claimed in any of Claims 1 to 5 wherein the injection of the aqueous suspension of the desired impregnant material into the gap is carried out through suitable holes or channels serving as inlets into the mould system, in one or both of the mating components of the mould.

7. Process as claimed in any of Claims 1 to 6 wherein the quantity of the suspension used is sufficient to fill substantially completely the gap within the mould, and the gap itself is equivalent in volume to the total accessible voidage of the foamed organic material.

8. Process as claimed in any of Claims 1 to 7 wherein the forcing of the impregnating suspension into the open-cell pores of the foamed material is achieved by simply by closing the inlet (feed lines) for the impregnant suspension and then moving the mating components of the mould together so as to diminish the internal gap which now contains the impregnant suspension and thereby force the impregnant suspension into the open cells of the foamed material.

9. Process as claimed in any of Claims 1 to 8 wherein the differential pressure across the foamed material is increased by applying suction or vacuum to the drainage channels or outlets.

10. Process as claimed in any of Claims 1 to 9 wherein the foamed organic material used has a basically closed-cell structure but also a multiplicity of inter-communicating interstitial gaps and spaces within it which can behave as the equivalent of an open-cell structured foam and be impregnated.

11. Process as claimed in Claim 10 wherein the foamed organic material is made by taking prefoamed beads or fragments of a polymer (for example foamed polystyrene) and bonding them together so that, although they adhere to each other sufficiently to form a mass of some reasonable strength, the beads or fragments are not pressed completely together and residual interstitial gaps and spaces are left which intercommunicate sufficiently to give the mass a permeability similar to that of a true'oPen-cell structure.

12. Process as claimed in any of Claims 1 to 1 j wherein there is used a resilient foamed material,. for example a cellular rubber or polyurethane.

13. Process as claimed in any of Claims 1 to 12 wherein the impregnant is concentrated selectively in localised areas for example at or near the surface of the foamed material.

14. Process as claimed in any of Claims 1 to 13 wherein the impregnant is an insoluble particulate inorganic material having a retarding or inhibiting effect on the melting, burning and/or vapourisation phenomena which occur when foamed materials are heated or ignited.

15. Process as claimed in any of Claims 1 to 14 wherein the impregnant is a layer mineral, for example a vermiculite, montmorillonite or bentonite.

16. Process as claimed in any of Claims 1 to 15 wherein the layer mineral has been chemically delaminated.

17. Process as claimed in any of Claims 1 to 1-6 wherein the particle size of the inorganic impregnant is in the range 50 to 100 microns, and preferably are of a shape having a high aspect ratio.

18. Process as claimed in any of Claims 1 to 17 wherein the impregnant is a delamindted layer mineral in the form of lamellae as small as practicable, preferably smaller than 50 microns and having high aspect ratios which are over 100:1.

19. Process as claimed in any of Claims 1 to 18 wherein the impregnant suspension contains from 10% to 50% by weight of solids.

20. Process as claimed in any of Claims 1 to 19 wherein there are used successive suspensions of different impregnants, so that one impregnant is predominantly located in the core region of the foamed material and another one is predominantly located at or near to the surface zones.

21. Process as claimed in any of Claims 1 to 20 wherein an excess of the impregnant is used, above that required for the interstitial penetration, to provide a surface layer of concentrated particles of the impregnant material, to provide a coating.

22. Process as claimed in any of Claims 1 to 21 wherein the impregnant material is wholly or partly organic in nature.

23. Process as claimed in any of Claims 1 to 22 wherein the foamed material which has been impregnated and dried is given a final treatment so as to modify or enhance it still further.

24. Process as claimed in Claim 23 wherein the final treatment is a heating treatment.

25. Process as claimed in Claim 23 wherein the final treatment is an after-coating treatment.

26. Process for making a composite foamed material substantially as described with reference to the accompanying drawings.

27. Composite foamed articles whenever made by a process as claimed in any of Claims 1 to 26.

28. Mould systems whenever adapted for the production of composite foamed materials by a process as claimed in any of Claims 1 to 26.