IE55150B1 - Dewatering process - Google Patents

Description

DESCRIPTION This invention relates to a foam treatment process for sheet materials and has particular reference to a process for reducing the water content of such sheet material.

Ways to reduce the water content of sheet material such as textile sheet material, are well known. The most widely used and oldest known method involves squeezing the sheet material between a pair of several pairs of mangle rollers. While certain constructions of mangles enable the water content to be reduced to low levels (e.g. 40 to 60% depending on the material to be treated), mangle-type equipment has several disadvantages. The higher the nip pressure the better are the mangling effects, but, of course, the deformation of the substrate by the nip pressure becomes more pronounced. - 2 - - 2 - 55150 Another drawback of the mangle principle is the lack of a simple, easily predictable correlation between nip pressure and the extraction effect. Using water content measuring instrument feedback to control and predetermine water retention levels is thus very difficult.

Another method frequently used is the vacuum extraction of water from textile sheet material. While it is possible to remove a certain amount of the water present in the interstices of the material, the friction between the vacuum slot and the moving sheet presents problems, particularly at high speeds, since adequate sealing become very difficult. Energy input thus may be too high in relation to the effects obtained (this is particularly true for all high speed operations).

Another method recommended for the removal of water from air permeable substrates is the blowing of air at very high air speeds against the surface of the moving sheet, usually at an angle of about 90° to the plane of the sheet. Energy input again is very substantial, and results vary greatly with the construction of the - 3 - - 3 - 55150 substrate (tightly woven/open weaves/nonwovens, etc.) while support of the sheet at a low level of friction may present serious problems, particularly in.the case of webs having a low cohesive strength.

All these known treatments which precede the final drying step are aimed at reducing the level of residual water prior to drying to lower the energy input required to remove the water still present at a 10 given dryer speed, and/or to increase the speed of the dryer and/or lower the drying temperature.

United States Patent Specification So. 4,062,721 describes and claims a method for removing water from 15 a wet fibrous sheet comprising the steps of mixing an aqueous slurry comprising mineral and binder, depositing said aqueous slurry on a wire mesh to form a wet sheet, adding a surfactant foaming agent to the slurry, said step of adding said surfactant foaming 20 agent being performed at substantially the time that said slurry is deposited on said wire mesh whereby essentially no internal foam is present in said wet sheet at the time of depositing, draining water from said wet sheet through said wire mesh, said drainage being aided by the force of gravity and draining 25 - 4 - additional water from said wet sheet through said wire mesh, said additional drainage being aided by air pressure differential created across the wet sheet whereby foam is generated within the wet sheet due to the passage of air therethrough.

This specification is concerned with the production of fire retardant felted mineral fibre panels and it is a feature of the invention that the generation of a foam should be confined to within the felted material itself. U-S. Specification No. 4,062,721 teaches with considerable emphasis, the importance of avoiding substantial foaming until the wet sheet is juxtaposed the air pressure differential created across the sheet.

We have found that if an air permeable sheet material is treated with a foam containing an agent capable of reducing the surface tension of the foamed liquid, then improved deliquifying of the air permeable sheet material, can be effected.

According to the present invention, therefore, there is provided a process for dewatering and/or cleansing an air permeable sheet material containing water and/or removable agents, which process comprises: (i) forming a foam liquid containing an agent capable of lowering the surface tension thereof, (ii) applying said foam to one side of the air permeable sheet material, (iii) causing the foam liquid to permeate the interstices of the sheet material by the application of a pressure gradient across said material, (iv) and removing the foam liquid and the water and/or removable agents from the other side of the sheet material, whereby the foam causes the water and/or removable agents to be removed substantially from between the interstices of the sheet material. - 6 - - 6 - 55150 In accordance with the present invention, the residual water may be removed even more effectively by blowing heated air of such volume and speed against one face of the wet air-permeable sheet material that the stream 5 of heated air penetrates to a substantial degree through the sheet material, i.e. exits therefrom on the opposing face at a speed and in a volume per minute which is at least 10% of the speed and volume blown against the other face.

The process of the invention is also extremely suitable for the lowering of the water content of wet double layers of sheet material, e.g. of two layers of textile fabrics.

This is particularly important because with a multiple layer processing e.g. of textile fabrics the process of the present invention provides at many finishing stages a very substantial saving in processing costs. - 7 - - 7 - 55150 The problems inherent in conventional methods for the water level reduction prior to drying become more severe in the case of multi-layer handling since, for example, the nip action of rollers becomes less 5 efficient and more complex, linear pressure in the nip (due to the compressibility of two superimposed more or less open structures) is smaller, and new problems arise, e.g. the formation of undesirable patterns (moire effects) and fibre entanglement between the two 10 layers if the nip pressures are as high as they have to be to at least come near the effects obtainable with single layer processing. These advantages of the system become, of course, even more important if multilayer sheet material such as 10 to 20 layers of 15 e-g. gauze fabrics, or multiple layers of sheet material with low physical integrity (such as non-wovens or paper) have to be processed.

The foam may be caused to permeate the interstices of the sheet material and may subsequently be removed therefrom by virtue of a pressure gradient applied across the material. - 8 - - 8 - 55150 In a particular embodiment of the present invention, a vacuum may be applied to one side of the sheet material which serves to "pull" the foam through the air permeable sheet to be treated.

In a particular aspect of the invention, a foam flow constraining substrate is in juxtaposition with the air permeable sheet material. This foam flow constraining substrate may be disposed on either side thereof.

In one embodiment, the foam flow constraining substrate is juxtaposed the surface of the air permeable sheet material remote from that to which the foam is applied. The foam flow-constraining and equalizing substrate may have in the wet state in air permeability lower than that of the wet air permeable sheet material. It is preferably in intimate contact with the surface of the air permeable sheet material not coated with foam, wherein the pressure gradient is of a magnitude sufficent to cause the foam to pass through both the air permeable sheet material and through the foam flow constraining substrate. - 9 - - 9 - B5150 The air permeable sheet materials which may be treated according to the present invention comprises woven, knitted and non-woven textile sheet material, paper at different levels of sheet formation (dewatering after the wet sheet has been formed, after dewatering treatments of other kinds), sheets of loose fibres (fibre stock in the form of webs, oriented or non-oriented sheets of loose fibres, i-e- in a layer having a thickness which is much smaller than the width, while the length is very large compared to the width, such as roving, sliver, webs produced by carding etc.). Textile fabrics may be present in single or multilayer configuration. As many as 16 layers have successfully been treated by the process of the present invention. Other airpermeable sheet material which may be dewatered by the process described may comprise a bed or layer of particulate matter, which is carried for instance on a porous conveyor belt (the foam flow-constraining substrate - 10 - - 10 -55150 may serve as such, or it may travel on a porous endless belt).

The airpermeable sheet material may be thin, i.e. have a low thickness, or be three-dimensional in the sense 5 that it consists or more than one layer of a thinner material as for example a gauze.

The airpermeable sheet material may be structured, i.e. it may consist of or contain structural elements 10 such as fibres or particles, clusters of fibres or particles with open spaces or voids between these elements, hereinafter referred to as "interstices" These structural elements may be bonded together by bonding agents, by hydrogen or other non-covalent 15 bonds, by covalent bonds, by mechanical interlacing or - 11 - - 11 -5 513 0 entanglement, or they may not necessarily be held together, particularly in the case of sheets or layers of particulate matter.

The air permeable sheet material may comprise natural material and/or synthetic polymers. The sheet material may typically be less than 30mm thick in the wet state, but thicker sheets may be treated if the airpermeability is sufficient to allow the foam to 10 permeate the structure at a reasonable rate and under the influence of the available pressure gradient.

The foam applied to the airpermeable sheet material is preferably aqueous, but it may contain if desired 15 non-aqueous liquids, e.g. in the form of an emulsion.

The foam contains an agent capable of reducing the surface tension of the -foam liquid and in the case of said liquid being water, said agent may be cationic, anionic, non-ionic, amphoteric surfactants (tensides), 20 or simply a non-surfactant lowering the surface tension of water when added thereto, e-g. alcohols (mono or polyhydroxy compounds), amines and amides. In certain cases it is desirable to remove such agents after dewatering, e.g. during drying. A volatile 25 agent may be used, i.e. an agent lowering the surface - 12 - - 12 -55150 tension of water which has a boiling point lower or close to the boiling point of water, which is carried off by water vapour; alternatively an agent may be used which decomposes at temperatures in the range of 5 50 to 100°C (i.e. during drying) or at temperatures above 100°C, preferably not higher than 200°C, during a heat treatement carried out during or after the drying step. Mixtures of different types of agents lowering the surface tension may, of course, be 10 employed.

Such volatile or heat-decomposable agents are usually used only for the last dewatering or washing step, since in intermediate steps it may be desirable to 15 re-use the liquid or foam/liquid mixture drained from the airpermeable sheet material, e.g. in the form of a system where lightly soiled liquid is used in foam form for the dewatering or washing of sheet material containing a higher concentration of soiling or 20 polluting agents, i.e. agents to be removed from the sheet material (counterflow washing concept). The presence of an agent reducing water surface tension in these cases is desirable because re-foaming (partial or complete, i-e- from a foam having a lower foaming - 13 - - 13 - 55150 ratio or from a largely air-free liquid) is necessary and should preferably be achieved without the addition of additional amounts of surfactants.

The foam may be produced in any convenience manner; e-g- static systems, which contain few, if any, moving parts, where foam essentially is produced by blowing into the liquid to be foamed through fine orifices to introduce tiny bubbles into water at predetermined air 10 to liquid rates, or dynamic systems, where air is beaten into a liquid by various systems involving rotating parts, e-g- rotating discs (usually serrated along the circumference) arranged on a shaft, one of these discs moving clockwise, the next 15 counterclockwise and so on, or other devices capable of introducing air into a liquid to produce a defined structure for the cells of the foam.

The size of foam cells should preferably be fairly 20 uniform, i-e- very large bubbles should not be present in small cell-sized foam since such a heterogeneous foam may give non-uniform and inconsistent results.

Generally speaking the largest cells present in the foam applied should not have a diameter larger than 25 the thickness of the layer of foam to be applied to - 14 - - 14 -55150 the airpermeable sheet material preferably it should be at most half the thickness of the layer. More uniform effects are obtained if the cell size is not larger than a quarter or preferably a tenth of the foam layer thickness deposited.

The concentration of agents capable of reducing the surface tension in the liquid before or during foaming obviously should be kept at the minimum necessary to obtain a foam of suitable foaming rate and foam stability.

The foaming rate is the ratio between the volume of the liquid after foaming to the volume of the liquid to be turned into a foam. A foaming rate of 10:1 thus means that the volume of the foamed liquid is ten times the volume of the unfoamed liquid. Foaming rates between 200:1 and 5:1 may be used, but a range between about 150:1 and 10:1 or preferably between 100:1 and 15:1 have been found most advantageous. The foaming rate obviously will determine the volume of foam to be applied if a given amount of liquid is to be used in the form of foam to dewater airpermeable sheet material. Thicker layers, i.e. higher foaming rates are desirable if the thickness of the sheet - 15 - - 15 - 53150 material varies due to its structure or surface texture. All surface features of the sheet material to be dewatered or treated should be immersed in the layer of foam to achieve uniform dewatering effects, 5 and thicker layers of foam may be applied if there is a considerable variation between the maximum and minimum thickness of the sheet material.

In one embodiment of the invention the foam applied to 10 the sheet material to be treated is caused to permeate into and through the structure and interstices between structural elements by causing a pressure gradient to form between the surface to which the foam was applied and the side remote therefrom, the pressure being 15 higher on the foam-coated side- Pressure applied from the side of the sheet material carrying the foam, or vacuum applied to the reverse side, or both, will force the foam to travel at substantially a right angle to the plane of the sheet material.

The use of vacuum has certain advantages over the use of pressure. It is easier to apply in a well defined area on the side opposite the foam location, the vacuum applying means (e.g. a vacuum slot) may be in direct contact with the substrate with no loss of 25 - 16 - - 16 - 55150 energy since essentially the vacuum acts only on the sheet material/substrate and the foam lying on the sheet material, with little or no air seepage from the outside Air pressure applied to the foam on the other hand is much more difficult to direct exclusively onto the foam and through the sheet material (some air will always be diverted due to the fact that the nozzle has to be above the surface of the foam layer). Foam is likely to be blown off in the surface of the sheet material instead of through it for the same reason. Removal, collection and draining of the foam/liguid exiting after permeation is much more difficult with air pressure. Another important advantage of vacuum as a pressure gradient-producing medium is the fact that a vacuum slot will stabilise the movement of the sheet material by holding it rather than causing it to flutter as a strong stream of air does. For these and additional reasons such as foam breakdown or a strong decrease of the foaming rate which can be produced by vacuum, but not (at least not to the same degree) by air pressure, and simple recycling of drained liquid/foam, the use of vacuum applied to the side of the air permeable sheet material not carrying the foam ~ 17 - ~ 17 - 5 515 0 is the preferred method for creating a pressure gradient and causing the foam to permeate into and through the sheet material.

The foam emerging from the downstream side of the sheet material is not identical to the foam as applied, since for instance, its foaming ratio is decreased by the water removed from the airpermeable sheet material. Depending on the properties of the 10 foam it may also be lowered by the permeation process.

It may be further decreased (which in many cases is desirable) by adjusting the stability of the foam to the minimum level desirable from the point of view of foam collapse between foam formation, foam deposition 15 on the sheet and the time permeation starts. Passage through porous substrates may also affect the size of foam cells and foam cell size distribution, i.e. the difference in the size of the smallest and the largest cells- Material and agents removed by the foam from 20 the sheet material may also affect the characteristics of the liquid or foam or foam/liquid mixture exiting from the sheet material. Generally speaking, it is desirable to have a low foaming ratio or substantially no foam in the vacuum slot, at least if the liquid is 25 to be discarded. But even if it is recycled, one may - 18 - - 18 -55150 have better control over the process if the drained foam or foam/liquid mixture is re-foamed to a predeterminable foaming rate.

In other cases it may be desirable to drain liquid essentially in the form of foam, i-e. to incorporate water removed from the sheet material into the foam permeating through it. In such cases the stability of the foam applied and the foaming ratio (which is lowered by the liquid drained from the sheet) may be suitably adjusted, i-e- the foam stability is increased, the foaming rate preferably being kept at such a level that the foam can be reapplied if desired even without refoaming. In many cases it may be desirable to reduce the foaming rate to virtually zero, i-e- to use conditions and equipment where liquid containing little or no air exits from the system. In this case one will reduce original foam stability.

In another embodiment of the present invention, a foam flow constraining substrate may be disposed in juxtaposition with the air permeable sheet material to support the same during the foam treatment. The foam flows constraining substrate is peferably juxtaposed - 19 - - 19 - 5 5 1 the air permeable sheet material on the side remote from that to which the foam is applied. In an alternative embodiment, however, the foam flow constraining substrate may be juxtaposed the air 5 permeable sheet material on the side thereof to which the foam is applied.

Whichever embodiment is employed where a foam flow constraining substrate is used, it is preferably a 10 sheet material having the following characteristics:- 1. Ensuring an essentially uniform permeation of air liquid and foam through interstices or pores in the sense that these pores are distributed evenly over 15 the surface of the substrate and that the maximum diameter or cross section of the pores are predeterminable and of known magnitude; if the size of the pores is not geometrically definable such as for instance in the case of a non-woven fabric then the 20 air and foam permeabilities may be determined by a large number of small pores and not by a relatively small number of large pores. 55150 - 19A- 2. Ensuring that the air permeability of the substrate material is at the most equal to that of the air permeable sheet material to be treated and preferably, at least 10% lower than the air 5 permeability of the air permeable sheet material. 3. Ensuring that the maximum diameter of these pores is preferably at the most, 50 microns, and more preferably not greater than 30 microns.

The uniformity of the maximum pore size in the foam flow constraining substrate results not only in_ 10 - 20 - - 20 - 55 150 constraint, but also in equalisation of the flow of foam through the sheet material and said substrate.

The substrate may be a woven fabric or a non-woven 5 web. The construction of the fabric or web should be sufficiently stable to retain the pore characteristics in use.

This is usually easier to achieve in the case of more 10 planar, i.e. less three-dimensional configurations as opposed for instance to knitted structures, which are not only more open, but tend to become distorted (with some pores becoming larger) if exposed to stress. Knitted fabrics for this reason were found to be less 15 suitable, unless the configuration of interlacing yarns and fibres is sufficiently stabilised by blocking fibre-to-fibre and yarn-to-yarn movement (such blocking may also be useful or even necessary in the case of unstable woven fabrics or webs), and 20 provided airpermeability and maximum pore diameters can be held at the levels specified above and below.

The pores or interstices through which the pressure gradient causes the foam to permeate through the 25 airpermeable sheet material and the foam - 21 - - 21 -55150 flow-constraining substrate, may be essentially round or square as in the case of a filter fabric, where pore size and pore shape is determined by the open space lying between yarn intersections (the yarn being very compact), or they may have oblong shapes, i.e. they may be formed by single fibres arranged in relatively parallel configurations, such as fibres forming a yarn with a relatively small number of turns per inch. It has been found that woven fabrics consisting in at least one direction of a yarn with a very low twist factor (i.e. few if any turns per inch), where fibres (preferably filament fibres) due to the low number of turns are arranged in an essentially parallel configuration relative to each other and again due to the low twist factor rather form an essentially two-dimensional ribbon or band instead of a three-dimensional yarn with a more or less circular cross-section, are particularly suitable among woven fabrics. Filter fabrics, i.e. fabrics of very tightly woven structures with very compact yarns are suitable due to the very accurate maximum pore size and the wear resistance of such fabrics. While pore size in the case of filter fabrics is defined by the open space between yarn intersections i.e. by the yarn diameter, yarn construction and fabric - 22 - - 22 - 5 515 0 construction, it is determined by the spacing of the essentially parallel filaments of the ribbon-like low or no twist yarns in the case of the other type of weave mentioned.

In many cases, other woven fabrics, i.e. fabrics containing either low or no-twist yarns, or filter fabric yarns, may be used provided their airpermeability is at most equal, preferably at least 10 10% lower than that of the sheet material to be dewatered, and provided maximum pore sizes are less than 50, preferably less than 30 microns. Cellulosic, cellulosic blend or synthetic fabrics have under these conditions given adequate dewatering effects.

Filter fabrics made of synthetic filament yarns with a mesh aperture of at most 50, preferably at most 30 microns are suitable for achieving good dewatering effects. If stationary filter plates are used to 20 constrain foam flow, best results are obtained if the maximum pore diameter is 40 microns, preferably 30 microns. Airpermeabilities of at most 4000, preferably at most 2500 litres/square meter/second give acceptable effects in the case of filter 25 fabrics. - 23 - - 23 -55150 In the case of woven fabrics consisting of yarns and fibres which do not give fabric structures with porosity features as well defined as filter fabrics, airpermeability has been found to be the best 5 criterion. Woven fabrics should have an airpermeability (measured in wet state at least if water-swellable fibres are present) of at most 250, preferably at most 200 litres per square metre per second (determined at a pressure equal to the weight 10 of a water column of 20 centimetres). Woven fabrics having an airpermeability of 100 l/sq.m./sec. or even 10 l/sq.m./sec. have given excellent results.

Nonwoven structures for use as the foam flow 15 constraining substrate having a maximum airpermeability of at most 2000, preferably at most 1000 litres per square metre per second give acceptable dewatering effects. It is preferred that the fibres of the web should be suitably spaced, the 20 pores (i.e. open space between fibres) should be distributed over the web in sufficient uniformity and the configuration of the interstices between fibres which define pore size should be sufficiently stable (i.e. if it does not change-affecting pore size and -24- -24- 55150 uniformity-under the influence of the pressure gradient and/or actual use).

Uniformity of pore distribution over the area of the 5 substrate and of maximum pore diameters is important because the foam flow-constraining substrate not only serves to constrain the flow of foam by causing the foam to flow through a large number of pores with a relatively uniform maximum pore diameter, but also 10 to equalise the volume of foam forced through the sheet material over its entire surface and the substrate by the pressure gradient in the sense that the thickness of the foam layer is reduced uniformly over the surface of the airpermeable sheet material, 15 i.e. that zero foam layer thickness is reached at virtually the same time all over the surfae of the sheet material. If in certain places foam would permeate substantially faster than in others, dewatering effects could become non-uniform because 20 due to the different flow-through properties of foam and air, the areas where zero thickness of the foam layer is reached first would act as by-passes, i.e. the residual foam on the other areas would permeate more slowly or incompletely, thus affecting the removal of water from the sheet material in those 25 - 25 - - 25 - 55150 areas. The foam flow-constraining substrate thus serves both to channel uniformly the flow of foam and to ensure that the pressure gradient, the flow of foam through the sheet material and hence the dewatering effect is uniform over the surface of the airpermeable sheet material even if the latter due to its structure or configuration should have non-uniform air or foam flow-through properties.

The foam flow constraining substrate may be in close contact with the sheet material to be dewatered, i.e. there should be no open space or gap between the sheet material and the substrate except open space determined by the surface texture of the two sheets, hence the pressure gradient should be acting through both sheets without any appreciable amount of air entering between the edges of the two sheets in the case of vacuum, or air escaping between the sheets if air pressure causes the pressure gradient to form.

In the preferred mode of the invention the airpermeable sheet material, to which a layer of foam is applied travels in close contact with the foam flow-constraining substrate, which thus carries the sheet material, for instance over vacuum slots 5 515 0 - 26 - producing the pressure gradient and which draws tne foam lying on top of the airpermeable sheet material through the latter and through the substrate underneath.

' This system not only has the advantage that an airpermeable sheet material having little or no mechanical integrity of its own may be treated easily, but that a delicate sheet material (i.e. material 10 sensitive to damage by friction) is not caused or allowed to rub against stationary surfaces such as the edges of a vacuum slot. At the same time the system is very versatile in the sense that optimum dewatering effects on sheet material of a wide range of 15 construction, configuration, airpermeability and bulk may be achieved simply by using a suitable foam flow-constraining substrate, by applying a suitable foam and adjusting if necessary the pressure gradient.

Foam flow-constraining substrates may comprise natural or synthetic fibres, blends or inorganic material such as glass or metal fibres or thin wires (wire mesh) provided it has an airpermeability lower than the sheet to be dewatered and preferably a maximum pore 25 size (mesh aperture) of at most 100 micron, preferably - 27 - - 27 -55150 lower than 50 micron or even lower than 30 micron. Perforated metal, perforated plastic sheet material, or woven material gauzes may be used provided the specifications mentioned above apply.

Such substrates may be arranged in the form of endless belts, or of rotary screens. Stationary filter plates may also be used if they meet specifications as regards maximum pore size, but the friction created 10 between the sheet material and the filter plate by the movement of the sheet material and enhanced by the pressure gradient may be disadvantageous. The permeability to air of the foam flow-constraining substrate should as mentioned above be lower than the 15 permeability to air of the wet sheet material to be dewatered (in the case of substrates consisting of or containing water-swellable fibres, one should determine the airpermeability in wet state).

Substrates having a very much lower airpermeability than the sheet material to be dewatered may give very good dewatering effects; in fact in most cases, for a given type of substrate, dewatering effects increased (i.e. residual water content decreased) with - 28 - - 28 - 55 150 decreasing airpermeability of the substrate as is shown in Table 1.

It is of course not possible to correlate directly 5 types of fabrics differing basically as regards their foam flow-constraining features, e.g. filter fabrics {where pores are defined by the yarm diameters and yarn spacing) to woven fabrics where the spacing of for instance low twist filamentous fibre material 10 arranged in ribbon-like fashion determines air and foam flow properties, or to nonwoven structures where the orientation, spacing and configuration of fibres and fibre intersections determine pore size. Furthermore, not only the airpermeability, but to an 15 even larger degree the pore size may influence the degree of water removal for a given sheet material.

In the case of filter fabrics (polyester, polyamide or other synthetic fibres), where air and foam flow 20 characteristics as well as pore size are almost exclusively defined by the diameter of the yarns used and hence the mesh count, dewatering performance follows very closely the mesh aperture and to a slightly lesser degree airpermeability as is shown in Table 1. - 29 - 55150 Table 1 31 32 Filte 46 c Fabric 39 No. 44 37 41 Residual Water After Dewatering (% owf) 130 140 170 180 185 195 195 Mesh aperture 25 26 100 58 80 53 80 Mesh count 184.5 165.7 58.5 110.5 74.5 120 81.1 Yarn diameter/cm 0.030 0.035 0.070 0.033 0.054 0.030 0.043 Open Surface % Air-Permeability 19 17 3 4 3.5 40 35.75 41 42.5 l/m2/s) Water Permeabi- 2100 1250 4400 4450 4400 5050 6000 ity, (l/m2/s) 485 265 780 — 770 850 950 The data set out in Table 1 above shows that among filter fabrics those with a mesh aperture higher than 20 30 removes substantially less water than fabrics with a mesh aperture below 30. The fabrics having the lowest mesh aperture also were those with the lowest air and water permeabilities, the highest mesh count and the lowest open surface. - 30 - - 30 - 55150 Such correlation between dewatering effect, mesh aperture, air permeability and mesh count and open surface of filter fabrics and filter plate was found for widely different airpermeable sheet material 5 ranging from tissue paper to nonwoven webs to cotton broadcloth and eight to sixteen layers of cotton gauze. In addition to a mesh aperture of at most 30 microns, a mesh count above 100, preferably above 150, an open surface below about 25, preferably below 20 10 and airpermeability of less than 3000 1/sq. m./sec. (litres per square metre per second) are factors ensuring a high rate of dewatering.

In certain cases one may, of course, have to 15 compromise as regards the dewatering effect/airpermeability or open area ratio, e.g. if sheet material is moving extremely fast, if it contains very high amounts of water or if for any other reason high permeability of the foam 20 flow-constraining substrate is desirable.

One may for instance prefer to use a more open structure of filter cloth at least in preliminary washing steps to achieve a high flow-through rate. 55150 - 31 - In the case of woven fabrics with characteristics not as well defined as in filter fabrics, the pore size as mentioned earlier may be determined as much or more by fibre to fibre spacing as by yarn intersection 5 spacing. But even among fabrics of widely different constructions, the structures with the lowest airpermeability give the best dewatering effects as is shown in Table 2. 32 10 15 20 25 Table 2 No. 10 3 11 13 18 14 Fabric Constr. Fibre Material Remarks Airperm. 1/m /sec. Resid. Water Content % Ribs Nylon, filling yarn with extre mely low twist factor 10 95 Twill Cotton 15 120 Plain Weave Polyamide parachute cloth, filament yarns, very light weave 200 130 Plain Polyester, 250 150 Weave staple fibre yarn Broad- Cotton 280 175 Cloth Plain Weave Polyester 300 195 similar to No.13 Nonwoven Polyester 1200 160 - 33 - - 33 - 55150 * Fabric dewatered: Nonwoven, air-tangled.

Since there are hardly any methods known for defining, let alone determining "pore aperture" for fabrics of 5 widely different construction, yarn characteristics, and yarn configurations, the airpermeability (determined in wet state if water-swellable fibres are present) is the most meaningful and universally applicable rating criterion as regards dewatering 10 effects obtainable.

Another method is the so-called bubble-point test used by producers of filter cloth to define "nominal pore size".

In the case of woven fabrics, for instance a nominal pore size (as determined by the bubble point test) of at most 30, preferably at most 20 gives the best dewatering effects if these fabrics are not filter type fabrics. - 34 - - 34 - 5 515 0 It is also a useful method for evaluating the effect of mechanical or other treatments which may be applied to improve the dewatering properties of a given fabric (such as calendering, and shrinking).

Nonwoven fabrics have been used with average results for dewatering, provided the configuration of fibres and fibre intersections are well fixed by proper bonding to avoid distortions leading to uneven pore 10 size distribution, and provided the web is uniform as regards pore size and pore distribution in the material. Such nonwovens which may be used to give average dewatering effects as shown in Table 2, since the average pore size may have much higher 15 airpermeability than conventional woven fabrics (but usually lower than filter fabrics).

In preferred embodiments of the present invention, the characteristics of the foam should be selected such 20 that:- 1. a foaming rate of the foam applied to the surface of the airpermeable sheet material of 300:1 to 5:1 may be used; better results may be obtained if this range is between 150:1 to 15:1, with abofit 80:1 to 20:1 being the optimum range for 25 - 35 - - 35 - SSI SO most applications. 2. The volume of foam applied to the sheet material and caused to permeate through it should be such that the foaming rate calculated from the weight of liquid initially applied in foamed form, the foaming rate of this foam and the liquid removed from the airpermeable sheet material is 10% to 80%, preferably 30% to 60% lower than the foaming rate of the foam originally applied. It is, of course, desirable to use as. little liquid for the dewatering as possible. Depending on the characteristics of the sheet material to be dewatered (evenness of the surface, thickness, openness, amount of water to be removed, time available for permeation, pressure gradient available), a high, medium or low foaming rate may be more advantageous. 3. In order to get good dewatering effects at low add-on and low foam volumes existing in the system, foam stability levels, foam volumes applied, foaming rates of the foam applied and pressure gradients used as well as the characteristics of the foam flow-constraining substrate should be selected in such a way that the actual foaming rate of the foam/liquid - 36 - - 36 - 55 150 mixture exiting from the foam flow-constraining substrate is less than 50%, preferably less than 20% of the foaming rate of the foam originally applied to the surface of the airpermeable sheet 5 material.

While the change of the foaming rate specified in 2. may be calculated, the change specified in this paragraph is actual, i.e. to be determined 10 by measuring the volume and the weight of the foam/liquid mixture before and after permeation.

This reduction of the actual foaming ratio may be increased by using a foam of low stability, a 15 relatively low foaming rate and pressure gradients and foam flow-constraining conditions conductive to a relatively high degree of foam breakdown. 4. If an even lower foaming ratio or practically no foam is desirable at the exit end of the system, the foaming rate may be further reduced by carrying the foam/liquid mixture under the action of the pressure gradient, preferably vacuum, 25 through a pipe or tube equipped with at least one - 37 - 5S1S0 venture having at least one segment where the cross-section of the tube or pipe narrows suddenly by at least 5% preferably at least 25% of the cross-section. Virtually untapered 5 narrowing sections, i.e. sections where the cross section narrows rather abruptly are more advantageous than long tapered sections.

. Good dewatering effects are obtained while 10 lowering foaming ratios, i.e. the volume of foam leaving the system, by adjusting the stability of the foam applied to the airpermeable sheet material to such a level that this stability expressed in terms of foam half-life is reduced 15 by at least 25%, preferably at least 50% by the passage through the sheet material and the associated foam flow-constraining substrate and by the dilution produced by the liquid removed by the treatment from the sheet material. This 20 particularly applies if vacuum is used to produce a pressure gradient.

"Half-life" as applied to foam in this specification means the time after which the 25 volume of a foam put into a beaker at 20°C has - 38 - - 38 - 55150 dropped to 50% of the original volume, half of the foam volume thus having collapsed.

Some of the reduction of foam stability may be 5 produced by the passage through the porous sheet material and the substrate, while some foam stability loss is due to the dilution occuring inside the wet airpermeable sheet material. In most cases foam stability loss, irrespective of 10 its cause, is a useful criterion for the selection of processing conditions, in particular of the stability of the foam originally applied. The stability is determined not only by the type and concentration of the agent reducing surface 15 tension present in the foam, but also by the foaming rate and to some degree by the shape and size of foam cells, in particular by their maximum size. This gives a wide range of options as regards the formulation of the foam and the 20 optimization of the formulation from the point of view of other criteria mentioned.

The magnitude of the pressure gradient depends on processing conditions and the sheet material to be 25 treated (i.e. time available for permeation; volume of - 39 - - 39 - 55150 foam applied per area, e.g. per square centimetre; structure, weight, density, thickness of the sheet material; and amount of liquid to be removed). Practically all the foam applied to the surface of the sheet material should be caused to permeate into, preferably all through the entire thickness of the sheet material.

The time of exposure of the airpermeable sheet material, to which foam had been applied, to the pressure gradient preferably is such that virtually all of the foam applied is caused to permeate through said sheet material. If, for some reason, a layer of foam is to be left, or if the action of the pressure gradient is to be terminated before all the foam has been removed from the surface to which it had been applied, the residual layer of foam may be removed, for instance, by scrapping or by suction.

Permeation of the foam through the sheet material under the action of the pressure gradient may proceed in one or several steps, with one or several applications of foam to the surface of the sheet material to be treated, with the same or a different type and the same or a different magnitude of the - 40 - - 40 - 55150 pressure gradient causing permeation of the foam. As mentioned before, the preferred method for causing permeation consists in applying vacuum to the wet airpermeable sheet material through the foam 5 flow-constraining substrate, which is in close contact with said sheet material and which by the action of the vacuum and the air-pore plugging action of the foam layer present on the surface of the airpermeable sheet material, is even more tightly contacted with 10 said substrate.

Vacuum for instance may be applied to the system by passing the foam flow-constraining substrate and the superimposed airpermeable sheet material across one or 15 several slots, such a "vacuum slot" comprising an enclosed area which is connected through a tube, pipe or duct to a vacuum-producing pump. Multiple vacuum slots may be arranged in a horizontal plane, a curve (preferably convex) or in a rotating drum, the sheet 20 material and the underlying substrate preferably travelling horizontally or at most at an angle of 90°, preferably at most 60° to the horizontal plane. While the most advantageous configuration consists in applying the pressure gradient, in particular vacuum, - 41 - - 41 - 55150 to the foam flow-constraining substrate having a lower and preferably a more even airpermeability than the airpermeable sheet material, and through this substrate to the airpermeable sheet material, one may 5 if desired apply foam to the foam flow-constraining substrate, which travels (preferably with the same speed) in close contact on the wet airpermeable sheet material, and apply the pressure gradient, in particular vacuum in such a way that the foam is made 10 to permeate through the substrate, then through the underlying sheet material to dewater the latter. This configuration as an alternative to the preferred one where the foam is applied to the airpermeable sheet material, may in certain cases also be used for the IS washing application described below, at least in some of a series of in-line dewatering steps. Dewatering effects are, however, inferior to those obtained by applying the foam to the air/permeable sheet.

The process according to this invention may also be used to remove agents from the air/permeable sheet material. Such agents may be chemical agents, particulate matter, liquids, solids or mixtures of such products including impurities of undefined composition. In these cases the foam applied to the 25 55150 - 42 - surface of the sheet material (or the substrate) acts as washing medium, which removes undesirable agents and at the same time dewaters the sheet material so that a second step under the same or different 5 conditions will be more effective as regards the agent removal effect. The air/permeable sheet material may be dry when foam is made to permeate it for the first time to remove agents, or it may be wet as in the case \ of dewatering. The foam applied may contain 10 surfactants particularly suitable for removing the undesirable agents present, and/or it may contain compounds capable of neutralising, emulsifying or dispersing the undesirable agents present in the sheet material.

In one aspect of the invention, the amount of water present in the air permeable sheet material is within ±25% of the minimum amount of water contained per unit measure, of substrate when a foam is caused or allowed to transit a substrate in foam form from one side to the 20 other, foam being withdrawn as such from the second side.

As in the case of dewatering, multiple treatments according to the invention may be carried out in the same or in a different configuration, under the same 25 or different conditions as regards the type, composition and properties of the foam used, the pressure gradient employed, etc. To obtain maximum cleaning effects, it is important to operate underconditions ensuring good dewatering effects 30 described for dewatering apply. - 43 - - 43 - 5 515 0 A further aspect of of the present invention is the inclusions within the foam of agents which interact with the airpermeable sheet material or with material carried therein. "Interacting" meaning reacting chemically with said material or components thereof, forming covalent or non-convalent bonds (such as hydrogen or Van der Waals bonds) or just agents for depositing in the interstices of the said sheet material.

Such interaction treatments may be carried out independently or in combination with agent removal and dewatering treatments.

The foam may be applied to a dry air permeable sheet material, in particular foam may be forced into the dry airpermeable sheet material to form an inner interface under conditions (in particular as regards the absorbency of the substrate for the liquid forming the foam cells), which enable foam transit through the substrate. This is particularly beneficial in cases where (i) foam collapse by water adsorption by the material of the airpermeable sheet material is to be prevented (i.e. if the water content of the - 44 - - 44 - 5 5 15 0 latter in the case of removal of undesirable agents or the application of agents is relatively low (dewatering thus being necessary only after agent removal or agent application); 5 (ii) if for other reasons a minimum amount of water is to remain in the airpermeable sheet material; (iii)if interaction with the material of the airpermeable sheet is desired to take place within its structure, i.e. if interaction is to 10 proceed at inner interstices (and if desired also at the surface interface), foam may be forced into the dry airpermeable sheet material to form an inner interface under conditions (in particular as regards the absorbency of the 15 substrate for the liquid forming the foam cells), which enable foam transit through the substrate.

In these circumstances, the foam thus applied may contain agents capable of producing the interaction 20 desired, or if such agents are applied subsequently, interaction will take place not only at the surface to which such agents are applied, but also internally at any inner interfaces which may be formed. Foam transition conditions are determined and achieved by 25 causing a sheet of foam of uniform thickness to - 45 - - 45 - 55150 permeate through the airpermeable sheet material under the action of a pressure gradient, the sheet material being exposed to the action of this pressure gradient only for such a period of time until the first foam 5 cells appear on the opposite side of the sheet material.

The foam flow-constraining substrate may be cleaned in order to remove particulate or fibrous debris carried 10 by permeating foam from the airpermeable sheet material into the substrate or already present in the foam when it was applied, by reversing the flow direction (using foam, water, spraying of water, air blown against the substrate) after the substrate has 15 been separated from the airpermeable sheet material.

Water, foam or air is thus pressed through the substrate from the side which had not been in touch with the sheet material, i.e. where the pressure had 20 been lower during the treatment according to the present invention. If water/soluble material has to be removed from time to time or after each cycle of foam permeation, washing may either proceed by reversing the flow direction or using the same 25 direction as before. If soiling or clogging by debris - 46 - - 46 - 55150 is very severe, one may use different foam flow-constraining substrates in-line, i.e. transfer the airpermeable sheet material from one substrate to another between treatments involving foam permeation.

Following is a description by way of example only of methods of carrying the invention into effect.

The following data demonstrate the strong beneficial 10 effects of the process of the present invention.

In the examples, the following explanations and abbreviations will be used.

FFCS: Foam Flow constraining substrate APSM: Air-permeable sheet material MEF (APSM) Blott-Paper (APSM) Tissue (APSM) 20 Gauze (APSM) 8 layers of surg. gauze, bleached and scoured,....

Broadcloth (APSM) Foam Formulations and Specifications ("Foam") Blow ratio; volume of foamed liquid to volume of 25 liquid before foaming - 47 - - 47 - 55150 Formulation; Agents present in liquid to be foamed Formulation A: 2 grams/litre of nonionic surfactant (Sandozin NIT cone, Sandoz) Formulation B: 1 gram/litre of same nonionic surfactant Formulation C: 0.2 grams/litre of same surfactant Foam Volume: Volume of foam (in ml) applied to surface of APSM before applying pressure gradient volume in ml per dm2. Dewatering Effect: Bath content of APSM after applying foam, creating a pressure gradient causing the foam to permeate through the APSM and the FFCS, and determining and comparing the weight of the APSM sample after this treatment to its weight before the treatment, expressed in %owf (% on the weight of the fabric).

Residual Water Content: Water content of APSM after dewatering treatment (as opposed to "original water content", i.e. water content before dewatering treatment).

Example 1 Effect of Presence of Foam in Multi-Layer Substrates (Woven Fabrics) Processing and handling of fabrics in the tests: Two or more superimposed layers of the textile fabrics - 48 - - 48 - 5S15G mentioned were treated in wet state (pure water) as follows (a) Hard squeeze in nip between rollers, double passage, i.e. mangling repeated 5 (b) same, light squeeze, one and two passages, (c) same, but foam applied to the layers of fabric (between layers) before same squeeze as in (b), only one passage.

The effects obtained are expressed in grams of fabric 2 plus residual water per 100 cm .

The presence of agents lowering the surface tension of water per se has been found to increase the effect 15 of known mechanical water removal systems such as squeezing in a nip etc., particularly if the water-removing treatment has to be mild from the point of view of mechanical action, e.g. mechanical pressure applied to the sheet material.

Applying such agents in a foam bath will, however, further reduce the residual water content to a very substantial degree as shown in the following Table 3. 55150 - 49 -Table 3 Non-woven, 2.15 oz/sq yard, 100% rayon Sample 1 two layers of the non-woven padded in pure water, squeezed gently in mangle Sample 2 padded in water containing agent 5 10 capable of lowering surface tension of water, squeezed on same mangle in same way as Sample 1 Sample 3 same treatment as for Sample 2, but foamed bath (same composition as padded bath) fed between the two layers of non-woven before squeezing.

Residual Water Content Sample 1 200 % 15 Sample 2 (0.25 % surfactant) 130 % Sample 2 (0.01 % surfactant) 180 % Sample 3 (0.25 % surfactant) 110 % Sample 3 (0.01 % surfactant) 160 % 20 Since in certain cases it is undesirable to have residual surfactants present on the sheet material after drying, it has been found that in such cases one may use surfactants decomposing under the influence of drying temperatures, or carried off by the evaporating 5S150 - 50 - water, or surfactants which have an evaporation temperature not much higher than water.

S51 SO - 51 -Table 4 100% 100% cotton cotton broad voile (2 cloth (2 layers) layers) cotton gauze (16 layers) (a) Hard squeeze 2 passages (b) Light squeeze one passage (b) Light squeeze two passages (c) (b) treated with foam one passage of treatment (b) 4.12 g 2,32 g 5,2 g 3,84 g 5.12 g 3,85 g 4,5 g 3,09 g 9,3 g 11,7 g 11,62 g 9,9 g The treatment (c) of a sample given the nip treatment (b) followed by the same nip treatment in presence of a bath of foam thus gave a residual water content - 52 - - 52 - 55150 considerably lower than either treatment (b) alone or the repeating of treatment (b), i.e. the presence of the foam in the fabrics during the squeezing treatment improved the squeezing effect very substantially even 5 though the treatment with foam had increased the water content beyond that of the wet material used for the test.

EXAMPLE 2 10 Influence of Air Pass-through Treatments Woven Multilayer Substrates_ The same samples as in Table 3 were after squeezing treated for 10 seconds thereafter with a relatively slow stream of air blown against one face of the 15 sandwiched fabrics. 55150 - 53 -Table 5 Broadcloch Voile Gauze (2 layers) (2 layers) (16 layers) 5 10 15 (b) one passage 5,2 g 3,88 g 11,72 g through nip (c) one passage 4,5 g 3,09 g 9,9 g (b) after squeezing treated with air (room) temperature) 4,95 g 3,60 g 11,5 g (b) after squeezing treated with air at 32°C 4,8 g 3,3 g 11,5 g (c) after squeezing treated with air (room temperature) 4,38 g 2,84 g 10,05 g (c) after squeezing treated with air (32°C) 4,28 g 2,42 g 9,94 g 20 - 54 - - 54 - 55150 These results show that the short treatment with air gives surprising results even if the air is at or only slightly above room temperature - irrespective of the number of layers present and even though rather low 5 air speeds are used.

In some cases water levels are reached even under these very mild conditions, which are cmparable to those obtained by very hard squeezing. Higher air 10 temperatures such as 60°to 80°C and somewhat higher air speeds (yet well below the very high speeds used in nozzles as recommended by certain equipment manufacturers) do of course give even better results even at shorter treating times. Air temperatures of 40 to 80°C are available at low.cost from heat recovery systems of tenter frames, curing ovens or other thermal treating equipment. Air or water at such temperatures was considered to be of little use hitherto.

EXAMPLE 3 Influence of Presence of Foam on Squeezing Effect: Multilayer Son-woven Substrates._ Procedure Non-woven substrates (rayon, entangles) were wetted in - 55 - - 55 - 55150 an aqueous bath containing small amounts (0.2 g/litre) of a non-ionic detergent. Control sample A was squeezed hard twice in sandwich form in the nip of a padding mangle. Control Sample A' was squeezed 5 lightly in sandwich form in the nip of a mangle.

Sample was treated exactly as samples A, but after the squeezing in the nip the same bath in foamed form was sucked through the squeezed fabric by means of a 10 vacuum slot.

Sample Bj was again treated as sample A, but a foamed bath of the same composition was fed into the space between two layers of the squeezed non-wovens before 15 the sandwich entered the same nip as for sample A, i.e. during the mechanical treatment (squeezing) additional liquid in foamed form was present in the wet non-wovens.

Sample B’^ was treated exactly as sample A', but after the light squeezing the foamed bath was sucked through the two layers by means of a vacuum slot. 515 0 - 56 - Sample B'^ was treated exactly as sample A', but after the squeezing, the foamed bath was introduced between two layers of the squeezed non-wovens before passing the foam filled sandwich through the same nip as for 5 sample A'. - 57 - - 57 - 55150 Table 6 Air treatment: 5 seconds, air temperature 42°C Sample Foaming Treatment % Water % Water Rate retained after Air owf Treatment A hard squeeze, 120 % 2 passages B1 30:1 same, then foamed bath sucked through 120 % 100 % B2 80:1 same squeeze sandwiched/foam 125 % 100 % inserted/squeeze as A A' - light squeeze 230 % - B'l 25:1 same, then foamed bath sucked through 135 % 110 % 50:1 same 120 % 100 % 70:1 same 110 % 70 % B2 25:1 same squeeze sandwiched/foam 120 % 110 % 50:1 inserted/squeezed 110 % 100 % as A' - 58 - - 58 - 55150 Table 6 shows that the sucking of the foamed bath through the wet material may reduce the water content by more than 50% (even though the foam actually adds water to the water already present) and the feeding of 5 the foamed bath between two wet fabrics before squeezing also reduces the water content even though here again the foamed bath actually increases the total amount of water present. The table also shows that a very short treatment with low temperature air 10 will further markedly reduce the water content.

A very important step of the procedure is to insert foamed liquid between layers of wet air permeable sheet material, and then causing the foam to penetrate 15 the sheet structure and remove liquid by passing the layers with foamed liquid sandwiched between the layers through the nip of pressure rollers, i.e. rollers running in contact under adjustable pressure. - 59 - - 59 -55150 The application of the foam may be by known methods (knife, roller, kiss coating, from a trough or from perforated tubes to one or multilayered sheet material such as fabrics -woven, knitted, non-woven - paper, 5 air permeable sheets of foam etc.)· The foam may be applied from one side, from both sides or between layers of the sheet material. The foamed liquid may be aqueous, containing small amounts of 10 foaming agents, or it may contain agents such as foam stabilizers, agents destabilizing foams at elevated temperatures, finishing agents. It may be applied cold or have a temperature above room temperature. In certain cases non-aqueous liquids may be used.

Known systems capable of removing water from wet material may be used,not only may the application of the foam be integrated into the permeation step, but the permeation process may be integrated into the 20 liquid elimination process. One may for instance apply foam between layers of multilayered sheet material (e.g. two, four or up to twenty layers of fabrics, the foam usually being applied between middle layers), and then the material passed through the nip 55150 - 60 - of a mangle, forcing the foam into the structure and eliminating liquid in the same treatment. - 61 - 55150 EXAMPLE 4 Influence of Presence of Foamed Bath on Water Removal (Non-Wovens)_ Table 7 5 Samples Foaming % Water Treatment retained owf A - 110* hard squeeze B1 30 : 1 100% same, then foam 10 sucked through B2 80 : 1 110% hard squeeze, foam fed into sandwich, same hard squeeze 15 A' - 230% light squeeze B’l 25 : 1 100% same, foam 50 : 1 90% sucked through 70 : 1 85% B,2 25 : 1 110% light squeeze, 20 foam 70 : 1 105% fed into sandwich same light squeeze - 62 - 59150 EXAMPLE 5 Water vs foam: Water sucked through APSM vs same volume of water in foamed form sucked through same APSM Table 8a 5 Dewatering Effect in % owf FjpCS APSM No. 10 Gauze (8) No. 10 MEF No. 10 Blott-P. No. 10 Tissue Formulation (1) Water sucked through (11) 115% (27) 115% (11) 120% (118)110% (11) 120% (104)200%1 (118)120% sane water (1) sucked through as foam (60:1) (11) 90% (27) 90% (11) 80% (118) 80% (11) 95% (104)150%1 (118) 90% (10) 78% Strong Mangling (11) 110% (27) 110% (11) 120% 018)120% ....... (10)138% Formulation A (1) 7 layers, other test with one layer 8b Influence on Surfactant in Water FFCS APSM No. 10 Blott P.

NO. lo MEF NO. 10 Gauze (8x) No. 10 Fibre Stock (2 layers of surgical cotton) Plain water sucked through (11) 160% (11) 280% (11) 130% (15) 280% Water + Surf. (Form-A) sucked through (11) 120% (11) 110% (11) 110% (15) 340% Fonn. A foamed (60:1) sucked through (11) 90% (11) 80% (11) 90% (15) 135% - 64 - - 64 - 55150 EXAMPLE 6 Influence of Mesh Aperture of the PPCS (Test 109)_ The influence of the mesh aperture of different FFCS on dewatering effects obtained on different substrates was investigated.

FFCS; Filter plates in Buchner funnels as model for FFCS APSM: Blotting paper (numbers trial No.) Tissue MEF Residual Water Content 15 Foam Specs with filter plate I (mesh ap. 40-100 micron) as FFCS with filter plate II (mesh ap. 16-40 micron) as FFCS with filter plate HI (mesh ap. 10-16 micron) as FFCS Blow ratio 60:1 Formulation A Foam Volume: 300 ml/ dm2 MEF (109) 180 % 100 % 75 % Blott P. (109) 115 % 95 % 85 % Tissue (109) 135 % 98 % 68 % |Gauze (111) .120 % 90 % 79 % - 65 - 55150 Same tests, FFCS No. 10 superimposed on filter plates X, II and III.

Filter Plate I Filter Plate II Filter Plate III MEF (109) 82 % 85 % 84 % Blott.Paper (109) 98 % 95 % 100 % Tissue (109) 80 % 85 % 85 % Gauze (113) 90 % 86 % 86 % The FFCS in direct contact with the APSM determines predominantly the dewatering effect.

MEF Blott.Paper Tissue Gauze Water content prior to dewatering 150 - 160 % 140 % 160 - 170 % 130 - 150 % Water content after Strong Mangling (2 passages) MEF 140 % Blott.Paper 95 % Tissue 135 % Gauze 105 % Example7 Influence of FFCS: Dewatering effect in % owf APSM Fibre Stock·*- MEF Blcrtt.Pap. Tissue MEF Formulation A Foam. Fate 60 : 1 FEES None No. 10 None No. 10 None No. 10 None No.10 None Wire-screen Dewat. Eff. 190¾ 138% 195% 85% 115% 98% 135% 80% 24% 66% ;Trial) (15) (15) (120: (120) (109) (109) (109) (109 X X two layers of surgical gauze dynamic test (continuous treatment) x - 67 - 55150 Example 8 Influence of blow ratio on dewatering effect 8a: FFCS: No. 10 (9) APSMtMEF Formulation A Volume of foam constant, weight of liquid variable.

Volume of foam 300 ml/dm2.

Blow ratio 300 150 100 75 60 50 38 30 Dewat. effect (a) 115 % 110 % 90 % 80 % 75 % 70 % 68 % 68 % Dewat. effect (b) 95 % 85 % 68 % 67 % 65 % 63 % 63 % 62 % (a) (b) low vacuum exposure time double vacuum exposure time of (a) 10 - 68 - j j 1 *) ο 8b: (12) FFCS: No. 10 APSM: MEF Formulation A Volume of foam varied, weights of liquid foamed constant (1 g/dm2) Blow ratio 450 400 300 200 50 Dew at. Effect 98% 90% 80% 82S 73% 8c: (10) FFCS: Mesh Apert. 40 - 100 micron APSM: Tissue, Blotting Paper, Formulation A Volume of foam constant, weight of foamed liquid variable Blow ratio 300 75 50 30 10 Blott.Paper Form.B - 100% 102% Form.C 102% 102% 92.% Tissue Form. B 75% - 75% 15 Form. C 80% - 78% la a 1 5 0 - 69 - 8d: FFCS, Mesh Aperture 40 - 100 APSM: Gauze (8x) Formulation A Foam volume constant (200 ml), weight of foam liquid varied Blow Ratio 200 165 120 60 40 20 weight of liquid 0,6g l,2g l,7g 3,4g 4,5g 9g Dewat. effect· 135% 132% 136% 125% 116% 110% - 70 - 5 ο 1 5 υ Example 9 Influence of Volume of Foam 9(11) 5 FFCS: No. lo AFSM: Blotting Paper MEF Gauze Formulation A Blow Ratio 60 : 1 Foam Volume (ml/dm2) Dewatering Effect (Resid. water % owf) Blott.Paper MEF Gauze 100 95 % 80 % 93 % 200 95 % 80 % 90 % 400 105 % 80 % 90 % 600 - 80 % - 700 80 % “ - 71 - 55150 9b]_(27) FFCS: No. 10 APSM: Gauze Formulation A Blow Ratio: 65 : 1 5 Foam Volume (ml/dm2) Dewatering Effect (Resid. Water owf) 100 92 % 200 91 % 300 90 % 10 400 σ\ GO 500 95 % 50 ml water (not foamed) 1X3 % - 72 - 9c: (118) FFCS : No. 10 APSM : MEF Blotting Paper Formulation A 3 Blow Ratio : 60 : 1 Foam Volume 700 (ml/dm2) 100 200 400 600 1 o Resid.Water (% owf) 80% MEF 80% 80% 80% 80% Blott. Paper 93% 94% 105% Residual Water Mangle-treated MEF 110% Blott. Paper 120% 15

Claims (31)

73 - 73 - 55150

1. A process for dewatering and/or cleansing an air permeable sheet material containing water and/or removable agents, which process comprises (i) forming a foam liquid containing an agent capable of lowering the surface tension thereof, (ii) applying said foam to one side of the air permeable sheet material, (iii) causing the foam to permeate the interstices of the sheet material by the application of a pressure gradient across said material, (iv) and removing the foam liquid and the water and/or removable agents from the other side of the sheet material, whereby the foam causes the water and/or removable agents to be removed substantially from between the interstices of the sheet material.

2. A process as claimed in claim 1 wherein the pressure gradient is provided by mechanically urging the foam through said material.

3. A process as claimed in claim 1 wherein the pressure gradient is established by providing pressure to the side of the sheet material to which the foam is applied.

4. A process as claimed in claim 1 wherein the pressure gradient is established by the application of a vacuum to the side of the sheet material remote from that to which the foam is applied. - 74 - - 74 - 5 5 15 0

5. A process as claimed in any preceding claim wherein the foam is in the form of an aqueous foam.

6. A process as claimed in any one of claims 1 to 5 wherein the foam is in the form of a non-aqueous foam. 5

7. A process as claimed in any preceding claim wherein the foam is in the form of an emulsion.

8. A process as claimed in any preceding claim wherein the agent capable of lowering the surface tension is one which decomposes at a temperature 10 within the range of 50°C to 200°C whereby the agent is removed during any subsequent drying or heat treatment.

9. A process as claimed in any preceding claim wherein 'the size of the foam cells is fairly uniform. 15

10. A process as claimed in any preceding claim wherein the maximum cell size of the foam is not more than 1/4 the thickness of the air permeable sheet material to which it is applied.

11. A process as claimed in any preceding claim wherein 20 the foaming rate of the foam applied to the sheet material is within the range of 300:1 to 5:1.

12. A process as claimed in claim 11 wherein the volume of foam permeating the sheet material is such that the foaming rate of the foam removed from 25 the air permeable sheet material after passage therethrough is 10 to 80 % lower than the foaming rate of the foam originally applied. - 75 - - 75 - 5S1 50

13. A process as claimed in any preceding claim wherein the operating conditions as regards foam stability, foam volume, foam rate, and foam pressure applied, are such that the foam emerging from the air permeable sheet is less than 50% of the foaming rate of the foam applied to the air permeable sheet material.

14. A process as claimed in any preceding claim wherein a foam flow constraining substrate is in juxtaposition with the air permeable sheet material to support the same during the foam treatment.

15. A process as claimed in claim 14 wherein the foam flow constraining substrate is juxtaposed the air permeable sheet material on the side remote from that to which the foam is applied.

16. A process as claimed in claim 14 wherein the foam flow constraining substrate is juxtaposed the air permeable sheet material on the side thereof to which the foam is applied.

17. A process as claimed in any one of claims 14 to 16 wherein the foam flow constraining substrate is arranged to move with the air permeable sheet material.

18. A process as claimed in any one of claims 14 to 17 wherein the foam flow constraining substrate is a sheet material having porous characteristics ensuring a substantially uniform permeation of air, liquid and foam through the interstices thereof, said substrate having an air permeability at least equal to the air permeable sheet material to be treated. - 76 -

19. A process as claimed in claim 18 wherein the dimension of pores or interstices of the foam flow constraining substrate is not more than 50 microns.

20. A process as claimed in any one of claims 14 to 19 5 wherein the foam flow constraining substrate is a woven fabric, a non-woven web, or a mesh.

21. A process as claimed in any one of claims 14 to 20 wherein the foam flow constraining substrate is a woven fabric having an air permeability of not more than 1o 250 litres per metre per square metre per second or a non-woven structure or mesh having an air permeability of not more than 2000 litres per metre per square metre per second.

22. A process as claimed in any one of claims 14 to 21 15 wherein said substrate is maintained in close contact with said sheet material throughout the treatment with the foam.

23. A process as claimed in any one of claims 14 to 22 wherein the foam is caused to permeate the 20 interstices of the sheet material by means of a pressure gradient, said pressure gradient being generated by means of a vacuum applied on the side of the air permeable sheet material remote from the side on which the foam is applied, said vacuum being applied by 25 passing the air permeable material across one or more vacuum slots, each vacuum slot being defined by an open tube pipe or duct connected to a vacuum producing pump. - 77 - 5150

24. A process as claimed in claim 23 wherein multiple vacuum slots are arranged in a plane, a curve, or within a rotating drum.

25. A process as claimed in claim 24 wherein said air permeable sheet material is caused to travel at an angle of not more than 60° to the horizontal plane when traversing said vacuum slot.

26. A process as claimed in any preceding claim wherein the foam includes one or more treatment agents for the removal of deleterious matter from said air permeable sheet material.

27. A process as claimed in any preceding claim wherein the foam additionally contains agents suitable for removing deleterious agents present and further contains compounds capable of neutralising, emulsifying, and/or dispersing deleterious matter or agents present in said sheet material.

28. A process as claimed in any one of the preceding claims wherein a further application of foam containing an agent capable of·lowering the surface tension is applied to the air permeable sheet material, said foam being caused to permeate the interstices of the sheet material in the manner claimed in any preceding claim and thereafter removing the foam and/or constituents of the foam from the sheet material. - 78 -

29. A process as claimed in any preceding claim wherein the foam liquid applied to the air permeable sheet material contains agents to be interacted with or deposited into said air permeable sheet material. 5

30. A process as claimed in claim 1 and substantially as described in any one of the specific examples herein before set forth.

31. Textile products whenever treated by the method as claimed in any preceding claim. MACLACHLAN & DONALDSON Applicants' Agents 47 Merrion Square Dublin 2