PROCESS FOR MAKING A FOAM COMPONENT

Abstract: The present invention relates to a process for making air stable, water-reactive foam components comprising polymeric material and an active ingredient and preferably a liquid, which are to be delivered to aqueous environment, using the step of submitting a viscous mixture of the ingredients, having a specific viscosity and/ or being intensively mixed, to pressure, typically by using an extrusion process, and whereby a gas is introduced in this mixture. The process is typically such that only small amount of liquid are required and only limited drying is needed to remove the liquid to obtain the components. Typically additional gas is injected in the process (in addition to gas of mixing) to improve foaming. The invention also provides components obtained by such a process.

Description: Process for Making a Foam Component Technical Field The present invention relates to a process for making foam components by subjecting a specific mixture of polymeric material, active material and preferably a liquid to pressure and introducing a gas by and subsequently shaping the mixture and removing the pressure. The invention also relates to components obtainable by such a process. Background to the Invention Compositions such as cleaning products, personal-care products, cosmetics and pharmaceuticals often comprise active ingredients which are sensitive to moisture, temperature changes, light and/or air during storage. Therefore, such ingredient actives are often protected by water-soluble coatings; for example enzymes are coated to protect them. Recently, there has been a trend to make various cleaning compositions but also personal cleansing and personal care compositions in unit dose form. For example detergent tablets are being used widely. A problem with many solid materials such as granules and unit dose compositions, is that they have a tendency to break up or form dust during handling due to physical forces. This creates problems for the user, for example, waste product is formed, and the dust can also cause hygiene and health problems. Again, coating of these solid materials can improve this problem to some extent. The problem with many coated granules or compositions is that they do not always exhibit sufficient impact resistance during handling. Thus for example, even when handling coated materials, dust is formed which causes health and hygiene problems. The inventor has found an improved method of protecting actives or unit dose compositions against braking during handling and forming dust. It was found that when the active material are formed into a specific water-reactive foam component formed from polymeric material, effective protection of the actives, against physical forces, but also other storage conditions such as moisture, temperature changes etc. is achieved, whilst also effective delivery to aqueous environments is achieved. It is known that foams can be made from polymers, typically by melting the polymers or by foaming a aqueous mixture of a polymer and drying the foam mixtures. The problem with the formation of foams by melting is that a high temperature is required; the problem with drying of foam mixtures is that also high temperatures are required or very long drying times are needed. Thus, both methods are not possible when handling an active material which is heat sensitive or volatile. Also, when long drying periods are required, the foams are not dried equally and the resulting foam is thus not homogenous. It is also known to freeze-dry foam solutions under vacuum, by exposing the foam mixtures to vacuum and freezing conditions for a long period; this does not always result in good foams and moreover, many active materials can not be subjected to a long period of vacuum or freezing conditions, for example volatile actives evaporate from the foam. The inventor now found a very effective method of making improved foam components, whereby typically only limited amounts of solvent are needed and no extreme temperatures are needed to form the foams. They found an improved process for making foams of viscous mixtures of polymeric material, active material and optionally small amounts of liquid (which is typically submitted to intensive mixing to reduce the viscosity) by submitting it to pressure and then shaping the compacted foam shapes under release of pressure, for example by extrusion. A gas is introduced in the process. The use of the pressure and the subsequent release of the pressure causes the gas to expand, to thus increase the level of foaming; more over, the release of pressure results in evaporation of the solvent or part thereof, thus drying the foam without the need of heating for long periods or with high temperatures or with vacuum freezing conditions. The mixture has a specific viscosity and/ or is intensively mixed, to get the required processability to allow pressuriseing, introduction of gas and shaping and to allow the formation of stable, and typically elastic or flexible foams. Hereby, there is no need for the use of large amount of liquids and thus no need for long drying times or extreme drying conditions. This process can be used to make a wide range of foam component, for example foams comprising certain actives only, for example enzymes, perfumes, or for example whole cleaning products, pharmaceutical products, personal-care products, cosmetic products and fabric-care products. The foam component obtained is very stable and flexible or elastic, and delivers the actives effectively to water. They have been found to be very impact resistant, thus resulting in reduced braking-up or abrasion during handling and reduced dust formation. Foam components incorporating liquid ingredients provide a convenient way to handle said liquids in a unit dose form, and also, the incorporation of liquids in this form of unit dose foam results in reduced migration or phase separation. Also, foam components with for example enzymes can thus be obtained which are safer and more efficient to handle. Summary of the Invention The present invention relates to a process for making a water-reactive foam component comprising a polymer matrix and an active material, which is active in water, the process involving: a) obtaining a viscous mixture of a polymeric material and an active material having a viscosity of at least 150 Pa.s at a shear rate of 1.7s "1 and/ or obtaining a viscous mixture and intensively mixing this mixture with a power/mass of at least 20W/gr, . preferably at least 30W/gr or even at least 50W/gr; b) introducing a gas or agent which forms a gas (at 25°C and atmospheric pressure); c) pressurising the mixture of b) with a pressure of at least 2 bar; and d) shaping the mixture of c) and releasing the pressure to obtain the foam component. Hereby, the mixture comprises typically a liquid, preferably a solvent for the polymeric material and/ or the active material and then, in step d) the liquid or part thereof is typically evaporated, preferably at least by the release of pressure. The process is preferably done by an extrusion process, involving intensive mixing to reduce the viscosity and to allow compaction under said pressure and allow shaping. The intensive mixing can introduce gas, but preferably additional gas or an agent, forming a gas at atmospheric pressure and 25°C, is introduced, as described herein after. The type or amount of liquid used may be such an amount that no additional drying steps are required, but an additional drying may be used, as set out herein, for example brief oven drying. The foam component obtainable by the process herein releases the active ingredient or part thereof upon contact with water, the component preferably partially or completely disintegrating, dispersing, denaturing and/ or dissolving upon contact with water. This foam component is preferable a flexible, elastic foam component. Preferably the active ingredients are cleaning actives, personal-care or cosmetic actives or pharmaceutical actives. Preferred are temperature-sensitive or volatile actives or moisture sensitive actives, including enzymes, bleach, perfumes. The foam component may preferably be in the form of granules, or in the form of a sheet, preferably such that it can be used as protective coating for the actives, or be further shaped in the required shape, or in the form of a solid object such as a tablet, sphere, block or other shape allowing easy handling of a unit dose of the composition. Detailed Description The process of the invention involves obtaining a viscous mixture of the polymeric material, active material and preferably a liquid, which either has a viscosity of at least 150Pa.s at a shear rate of 1.7 s "1 (at 25°C) or which is intensively mixed as defined herein after, (thereby preferably obtaining a viscosity as specified herein), so that it is such that it can be pressurized and shaped. The intensive mixing is preferred to allow introduction of the gas or agent and / or to allow shaping. The mixture preferably has a viscosity (at 25°C) of at least 200Pa.s or even at least 250Pa.s or even at least 300Pa.s or even at least 350Pa.s, measured at a shear rate of 1.7 s " Preferably, the viscosity is such that measured (at 25°C) at a shear rate of 10.0 s "1 , the viscosity is at least lOOPa.s or even at least 150Pa.s or even at least 200Pa.s or even at least 250Pa.s. More preferably, the viscosity is also such that measured (at 25°C) at a sheer rate of 100.0 s "1 , the viscosity is at least 12Pa.s or even at least 16Pa.s or even at least 20Pa.s or even at least 28Pa.s. As set out above, the viscous mixture is either of the viscosity above or the viscous mixture is intensively mixed, to make the viscous mixture processable in the process of the invention. Preferably the mixture has the viscosity as specified herein and is also intensively mixed, as specified herein. Intensive mixing when used herein means mixed with a power/mass of at least 20W/gr, preferably at least at least 30W/gr or even at least 50W/gr or even at least lOOW/gr or even at least 200W/gr or even at least 250W/gr, preferably up to lOOOW/gr or even up to 500 /gr. The pressure used is preferably at least 5 bar or at least 10 bar or even at least 15bar. Preferably, the pressure used is up to 300 bar or even up to 250 bar or even up to 100 bar or even up to 50 bar. Preferred mixers used for this intensive mixing process are also capable of applying the required pressure; preferred are known extruders. A gas or an agent which forms or is a gas at atmospheric pressure and 25 °C is introduced in the mixture. This may be gas introduced by the intensively mixing. Preferred is however, that an additional gas or agent, forming a gas, is introduced to aid foaming, i.e. by further physical foaming and or chemical foaming. This can be done by any known method, but preferred are: - physical foaming by gas injection (dry or aqueous route), gas dissolution and relaxation including critical gas diffusion (dry or aqueous route); - chemical foaming by in-situ gas formation (via chemical reaction of one or more ingredients, including formation of carbon dioxide by an effervescence system). Also steam blowing and/ or UN light radiation curing can be used. It should be understood that the viscosity of the viscous mixture used in the process of the invention, as defined herein above, is of the viscous mixture as determined prior to incorporation of the gas or agent. Preferred gasses injected into the mixture include nitrogen, carbon dioxide or mixtures thereof , such as also air. The agents herein can for example be pressurised gasses, or super critical fluids, such as liquid nitrogen or preferably carbon dioxide. If the polymeric material and the active material are both solid, the mixture comprises a liquid, in order to obtain a viscous mixture. However, even if the mixture of the active and the polymer is already a viscous mixture, it is still preferred to add a liquid. Also preferred may be to add viscosity modifiers, such as thickening agents or hydrotropes, to obtain the required viscosity. The liquid, as described herein after in more detail, is preferably a solvent capable of dissolving the polymer and/ or active material or part thereof. Typically the polymeric material is water-soluble and the liquid comprises at least water. It may be preferred that the liquid is a mixture of materials, for example a mixture of water and an organic solvent, capable of lowering the boiling point of water. The amount of liquid used is preferably kept as low as possible, to reduce the need of drying of the foam component or to allow the sue of milder drying conditions. The amount of added liquid, or preferably solvent, in the is typically from 10% to 50% by weight of the mixture, more preferably from 15% to 45% or even 40% by weight, or even from 20% to 40% or even 35% by weight. It may be preferred that (by weight of the liquid) 50% or more, or even 60% or more or even 80% or more of the added liquid is water. It may even be preferred that all of the added liquid is water The polymeric material and active material are preferably homogeneously dissolved or suspended within the solvent and the amount of liquid is thus selected accordingly. The level of the added liquid (solvent) in the resulting foam component is preferably up to 15% by weight, more preferably up to 10% or even up to 5% by weight. It may be preferred that at least some liquid remains present for example at least 1% or even at least 3% by weight. In the process herein, the mixture is submitted to pressure followed by (simultaneously or subsequent to one another) shaping the mixture into any required shape and removing the pressure or part thereof. Hereby, the gas present expands or the agent forms a gas and a foam matrix is obtained, i.e. forming spacings which are the areas inside cells of the matrix of the foam component. Also, by releasing the pressure, the liquid or part thereof evaporates, to thus form spacings which are the areas inside cells of the matrix of the foam component. A preferred process herein is an extrusion process. Hereby it is preferred that the polymeric material, active ingredient, gas or agent described herein and typically liquid, preferably including a solvent such as water, are introduced into an extruder (as a pre- formed mixture, or preferably as separate ingredients), wherein the ingredients are intensively mixed; then, the pressure is dropped at the exit point where the extruded mixture exits the extruder and is thereby shaped, whereby the liquid or part thereof evaporates (when leaving the exit point, it can be formed into the desired form, for example granules or sheets, or this may be done at a later stage, for example after a further treatment step such as drying). This results in formation of cells with spacings, as described herein after in more detail, which then may contain a gas, preferably air, and optionally the active ingredient. These spacings form the internal area of the cells of the matrix of the foam component of the invention. The formation of these spacings are partially responsible for the excellent flexibility of the foam components obtainable by the process of the invention. The level of polymeric material in the mixture is preferably from 10% to 60% by weight, more preferably from 15% to 50% by weight or even from 20% or even 25% to 45% by weight of the mixture. The final foam component comprises preferably at least 10% by weight of the polymeric material, more preferably from 10%> or even 20% or even 30% to 70%, or even to 60% or even to 55% or even to 50% by weight. The level of active material in the mixture is preferably from 10% to 60% by weight, more preferably from 15% to 50% by weight or even from 20% to 45 % by weight of the mixture. The final foam component comprises preferably at least 10% by weight of the active ingredients, more preferably from 10% to 70% or even from 15% to 60% by weight. As described herein, it can be useful that the foam component comprises a plasticiser and/ or a stabiliser to improve foam formation and stabilisation. Preferred is that at least a plasticiser is present in the mixture. Preferred are levels of from 3% to 25% by weight, more preferably from 5% to 20% by weight or even from 8% to 18% by weight (of the mixture) of plasticiser and or stabiliser. In the process, the mixture may be mildly heated, up to for example temperatures from 40°C to 70°C, preferably only up to 60°C or even 55 °C, to improve the shaping and to cause the liquid or part thereof to evaporate more efficiently. Typically, the temperature of the mixture is below the melting point of the polymeric material and preferably up to a temperature below the boiling point of the liquid (liquid at atmospheric pressure). The amount of liquid and process conditions to be used, can be chosen such that no additional drying of the foam is needed. However, it may be preferred to obtain an ever drier foam component. Then, the steps of the process herein may be followed by an additional drying step to further remove excess liquid, such as water, which may still be present. The drying step is typically to be done such that the final foam component is of about the same volume after the drying step as before the drying step. Thereto, the drying step is preferably done by freeze-drying, whereby the solvent, e.g. water, is removed under vacuum and reduced temperatures, for a short period of time. More preferred even is slow oven drying at modestly increased temperatures; the conditions depending on the size of the foam component, for example preferred are drying conditions of 40-70°C, or even 40-60°C for a short period of time, for example up to 3 hours, preferably up to 2 hours or even up to 1 hour, or even up to 30 minutes or even up to 20 minutes. Foam Component The foam component obtainable by the process of the invention has a matrix formed from the polymeric material or part thereof, and optionally other materials. The matrix is preferably such that it forms an interconnected network of open and/ or closed cells, in particular a network of solid struts or plates which form the edges and faces of open and/ or closed cells. The spacing inside the cells can contain part of the active ingredient and/ or a gas, such as air. The polymer material and the active ingredient may preferably be homogeneously mixed, in which case a so-called monophase or homogeneous foam component is obtained, which has uniform physical and chemical properties. However, it may be preferred that the foam component has different regions which are each a mono-phase, formed from homogeneous mixture and that thus the foam component as a whole is not homogeneous. 'Air-stable' or 'stable upon contact with air' when used herein, means that the bulk volume of the foam component substantially remains the same when exposed to air. This means in particular that the foam component herein retains preferably from 75% to 125%) or even from 90% to 110% or even from 95% to 100% of its bulk volume when stored in an open beaker (9 cm diameter; without any protective barrier) in a incubator under controlled ambient conditions (humidity = RH 60%, temperature = 25°C ) for 24 hours. Preferably the foam component retains from 75% to 125% or even from 90% to 110% or even from 95% to 100% of its bulk volume under the above storage conditions whereby the humidity is 80%. The bulk volume change can be measured by any conventional method. In particular useful is a digital image recorder system containing a digital camera coupled to a personal computer itself equipped with a calibrated image analyser software. A 1cm 3 specimen of the foam component is obtained and introduced in an open beaker having a diameter of 9 cm and stored for 24 hours at the above conditions. After 24 hours, the size in all three dimensions is measured with the image analysis recorder system. Each specimen measurement is repeated three times, and the average bulk volume change is calculated in %. Preferably, the foam component is such that, when in the form of particles of a mean particle size of 2000 microns or less, these foam component particles also retain from 75% to 125% or even from 90% to 110% or even from 95% to 100% of their bulk volume. This can for example be measured by placing 20 grams of the foam component particles, or a weight comprising more than 500 particles, in a volumetric beaker having a diameter of 9 cm. The beaker is taped lightly on its base until the foam component particles re-arrange themselves in a stable position with a horizontal top surface. The volume is measured. The open beaker with the foam component particles is then carefully placed in the incubator for 24 hours, set to the desired %RH and temperature. The bulk volume after the 24 hours is measured and the change of bulk volume is calculated in %. ' The foam component herein is unstable when brought into contact with water. This occurs such that the active ingredients or part thereof, present in the foam component is delivered to the water. Preferably the foam component or part thereof denatures, disintegrates, preferably disperses or dissolves in water. It may be preferred that the active ingredient is delivered rapidly and that the foam component is such that the polymeric material of the foam component disperses or dissolves rapidly, preferably at least 10% of the polymeric material, by weight, is dissolved or dispersed in 30 minutes after contacting the foam component with the water., more preferably at least 30% or even at least 50% or even at least 70% or even at least 90% (introduced in the water at a 1% by weight concentration). It may even be preferred that this happens within 20 minutes or even 10 minutes or even 5 minutes after contacting the foam component with the water. The dissolution or dispersion can be measured by the method described herein after for measuring the dissolution and dispersion of polymers. Preferably the water-unstable foam component is such that the total volume of the foam component is changed, preferably reduced, with at least 10%, compared to the initial total volume, as for example can be determined when 1 cm 3 of a foam component is added to 100 ml of demineralised water upon and stirred for 5 minutes at a speed of 200rpm, at a temperature of 25 °C. Preferably the change, or preferably reduction, in total volume is at least 20% or even at least 40% or even at least 60% or even at least 90% or even about 100%, e.g. because it may be preferred that substantially the whole foam component is disintegrated, dispersed or dissolved into the water quickly. This can be measured by use of any method known in the art, in particular herein with a method as follows (double immersion technique): 1 cm 3 of a foam component is obtained and introduced in a 100 ml micro volumetric measuring cylinder which is filled with 50 ml ± 0.1ml of an organic inert solvent. Acetone is for example used when found to be neither denaturing and/or not interacting with the polymeric material in the foam component, for example when this is PNA. Other neutral organic medium can be used according to the nature of the foam under investigation; the inert solvent is such that the foam component is substantially not dissolved, dispersed, disintegrated or denatured by the solvent. The cylinder is air sealed and left to rest for 1 minute so that the solvent penetrates the whole foam specimen. The change in volume is measured and taken as the original volume N,- of the foam specimen. The foam specimen is then removed from the solvent and left to dry in air so that the solvent evaporates. The foam specimen is then placed in a 250 ml beaker containing 100 ml of demineralised water, maintained at 25°C, under stirring at 200 rpm with the help of a magnetic stirrer, for 5 minutes. The remaining of the foam component specimen is filtered off with a 60mm mesh copper filter and placed in a oven at a temperature and for a period such that residual water is removed. The dried remaining foam component is re-introduced in the measuring cylinder which volume of acetone had been re-adjusted to 50 ml. The increase in total volume is monitored and taken as the final volume of the foam specimen Ny.. The decrease in total volume ΔN of the foam specimen is then: %ΔF = ^ * 100 Vi The foam component has preferably a relative density φ f * oam of from 0.01 to 0.95, more preferably from 0.05 to 0.9 or even from 0.1 to 0.8 or even from 0.2 to 0.7. The relative density is the ratio of the density of the foam component to the sum of the partial densities of all the bulk materials used to form the foam component, as described below: rfoam Hfoam Pfi where p is the density, and χ { is the volume fraction of the materials i in the foam components. It is preferred that the foam component is a flexible foam component. In particular, this means that the flexible foam component reversibly deforms, absorbing the energy of impacts or of forces so that the foam component remains substantially its original bulk volume after the physical force seizes to be applied on the component. In particular this means that when a foam component sample having a cross section of a specific length, for example 1cm, is compressed with a static force applied along the axis of that cross section, the static force being variable but at least equivalent to twice atmospheric pressure, the change of this length after removal of the force is at least 90% to 110% of the original length. This can for example be measured by use of Perkin-Elmer DMA 7e equipment. Similarly, the foam component is preferably flexible to such an extend that when a foam component sample having a cross section of a specific length, for example 1cm, is stretched with a static force applied along the axis of that cross section, the static force being variable, but at least equivalent to twice atmospheric pressure, the change of this length after removal of the force is at least 90% to 110% of the original length. This can for example be measured by use of Perkin-Elmer DMA 7e equipment. The flexibility of a foam component can also be reflected by the Young's or elastic modulus, which can be calculated from strain or stress mechanical tests as known in the art, for example by using Perkin-Elmer DMA 7e equipment following the manufacturer's experimental procedure. For example a foam component of 1 cm 3 can be used in the testing with this equipment. In particular, when using this equipment, the static forces applied along the axis of a cross section of a 1 cm 3 foam component are gradually increased until the deformation of the component, in the direction of the cross section, is 70%. Then, the force is removed and the final deformation of the foam component in the direction of the cross section is measured. Preferably, this length of the cross section after this experiment is preferably from 90% to 110% of the original length of the cross section, preferably from 95% to 105% or even from 98% to 100%. The foam component herein preferably has an elastic modulus or Young's modulus of less than 10 GN.m "2 , even more preferentially less than 1 GN.mf 2 , as measured with the Perkin-Elmer DMA 7e equipment. Preferably the polymeric component has a relative yield strain greater than 2%, and preferably greater than 15% or even greater than 50%, as measured with the Perkin-Elmer DMA 7e equipment. (The yield strain is in this measurement the limit deformation of a foam component at which the component deforms irreversible). The elastic modulus or Young modulus is related to the relative density, namely where p* and p s are as described above and Ε* is the Young's modulus of the foam component, and E s that of the polymeric material. This means that even stiff polymeric materials, with a high E s can be made into relatively flexible foams, by modifying the density thereof, in particular by introducing more gas in during the foam making process or by using additives, such as plasticisers at adjusted levels. The foam component preferably also comprises additional ingredients to improve (the performance of) the foam, for example to strengthen the foam component or make the foam component more stable, or more flexible or more water-soluble or water- dispersable, or which provide a better appearance of the foam, for example to colour or bleach the foam component. Preferred are plasticisers, stabilisers, dissolution agents as described herein after. Some of the preferred stabilisers, dissolution aids and plasticisers can have dual functionality, for example both plasticising and stabilising the foam component of the invention. The foam component herein preferably comprises a stabilising agent, which is typically capable of stabilising the active ingredient of the foam component herein, this is especially preferred when the active ingredient(s) comprise an oxidative or moisture sensitive active ingredient, such as one or more enzymes, perfumes and/ or bleaching agents. The stabilising agent may also stabilise the matrix of the foam component herein, and thus indirectly stabilise the active ingredient. The stabilising agent is preferably a compound which stabilises the active ingredient, or matrix, from oxidative and/or moisture degradation during storage. The stabilising agent may be, or comprise, a foam or a matrix stabiliser. The stabilising agent may be, or comprise, an active ingredient stabiliser, especially an enzyme stabiliser. Preferred foam stabilisers comprises one or more anionis or cations such as mono-, di-, tri- valent, or other multivalent ions, preferred are ions of the following metals: sodium, calcium, magnesium, potassium, aluminium, zinc, copper, nickel, cobalt, iron, manganese and silver; preferably these cations have a counter ions one or more of the following anions: sulphate, carbonate, oxide, chloride, bromide, iodide, phosphate, and nitrate, and combinations thereof. The foam stabiliser may comprise finely divided particles, preferably finely divided particles having an average particle size of less than 10 micrometers, more preferably less than 1 micrometer, even more preferably less than 0.5 micrometers, or less than 0.1 micrometers. Preferred finely divided particles are aluminosilicates such as zeolite, silica, or electrolytes described hereinbefore being in the form of finely divided particles. The foam stabiliser may comprise agar-agar, sodium alginate, sodium dodecyl sulfate, polyethylene oxide, guar gum, polyacrylate, or derivatives thereof, or combinations thereof. The foam stabiliser may comprise anionic or nonionic proteins or phospholipid-protein complexes. The foam component as a whole, or the active material prior to introduction into the foam component, may also be coated with a layer of a (polymeric) material, not being in the form of a foam as defined herein. Preferred coating agents include PNP (and derivatives thereof) and/ or PEG (and derivatives thereof) and PNA (and derivatives thereof) or mixtures of PNA with PEG and/ or PNP (or derivatives thereof); glycerol or glycerine, glycol derivatives including ethylene glycol, digomeric polyethylene glycols such as diethylene glycol, triethylene glycol and tetraethylene glycol, polyethylene glycol with a weight average M.W. of below 1000, wax and carbowax, ethanolacetamide, ethanolformamide, triethanolamine or acetate thereof, and ethanolamine salts, sodium thiocyanates, ammonium thiocyanates, polyols such as 1,3-butanediol, sugars, sugar alcohols, ureas, dibutyl or dimethyl pthalate, oxa monoacids, oxa diacids, diglycolic acids and other linear carboxylic acids with at least one ether group distributed along the chain thereof, water or mixtures thereof. Preferred active stabilisers comprise boric acid and salts thereof, and formic acid and formate salts and acetic acid and acetate salts, preferably calcium and/ or magnesium salts thereof. Active stabilisers suitable for use herein, especially when the foam component herein comprises a bleach, comprise anti-oxidants and/or reducing agents such as thiosulphate, methionine, urea, thiourea dioxide, guanidine hydrochloride, guanidine carbonate, guanidine sulfamate, monoethanolamine, diethanolamine, triethanolamine, sodium glutamate, bovine serum albumin and casein, tert-butylhydroxytoluene, 4-4,- butylidenebis (6-tert-butyl-3 -methyl-phenol), 2,2'-butlidenebis (6-tert-butyl-4- methylphenol), (monostyrenated cresol, distyrenated cresol, monostyrenated phenol, distyrenated phenol, 1,1 -bis (4-hydroxy-phenyl) cyclohexane, or derivatives thereof, or a combination thereof. Active stabilisers suitable for use herein may comprise sugars. Typical sugars for use herein include those selected from the group consisting of sucrose, glucose, fructose, raffinose, trehalose, lactose, maltose, derivatives thereof, and combinations thereof. It may be preferred that the active stabiliser is in the form of a coating or barrier which at least partially encloses the foam component herein or the active ingredient thereof, preferably completely encloses the foam component herein or the active ingredient thereof, especially an enzyme. The foam component herein may comprise (by weight) from 1%, or from 2%, or from 5%, or from 7%, or from 10%, or from 15%, or from 20% stabilising agent, and may comprise (by weight) to 70%, or to 60%, or to 50%, or to 40%), or to 30%, or to 25% stabilising agent. The amount of stabilising agent present in the foam component depends on the amount and type of the active ingredient and on the amount and type of the matrix herein. The foam component of the invention may also comprises a dissolution aid. The dissolution aid may preferably comprise a sulfonated compound such as C,-C 4 alk(en)yl sulfonates, C r C 4 aryl sulfonates, di iso butyl benzene sulphonate, toluene sulfonate, cumene sulfonate, xylene sulfonate, salts thereof such as sodium salts thereof, derivatives thereof, or combinations thereof, preferably di iso butyl benzene sulphonate, sodium toluene sulfonate, sodium cumene sulfonate, sodium xylene sulfonate, and combinations thereof. The dissolution aid may comprise a - alcohol such as methanol, ethanol, propanol such as iso-propanol, and derivatives thereof, and combinations thereof, preferably ethanol and/or iso-propanol. The dissolution aid may comprise a C 4 -C 10 diol such as hexanediol and/or cyclohexanediol, preferably 1,6-hexanediol and/or 1,4-cyclohexanedimethanol. The dissolution aid may comprise compounds which are capable of acting as whicking agents, such as cellulosic based compounds, especially modified cellulose. The dissolution aid may comprise swelling agents such as clays. Preferred clays are smectite clays, especially dioctahedral or trioctrahedral smectite clays. Highly preferred clays are montmorillonite clay and hectorite clay, or other clays found in bentonite clay formations. The dissolution aid preferably comprises an effervescence system. A preferred effervescence system comprises an acid source capable of reacting with an alkali source in the presence of water to produce a gas. The acid source may be any organic, mineral or inorganic acid, or a derivative thereof, or a mixture thereof. Preferably the acid source comprises an organic acid. Suitable acid sources include citric, malic, maleic, fumaric, aspartic, glutaric, tartaric succinic or adipic acid, monosodium phosphate, boric acid, or derivatives thereof. Citric acid, maleic or malic acid are especially preferred. The molecular ratio of the acid source to the alkali source present is preferably from 50:1 to 1:50, more preferably from 20: 1 to 1 :20 more preferably from 10: 1 to 1 : 10, more preferably from 5:1 to 1:3, more preferably from 3:1 to 1:2, more preferably from 2:1 to 1:2. It is highly preferred that the foam component comprises a plasticiser. Preferred plasticisers are selected from glycerol, ethylene glycol, diethyleneglycol, propylene glycol, sorbitol and mixtures thereof. Colouring agent to colour the foam component such as iron oxides and iron hydroxydes, azo-dyes, natural dyes, are also preferred , preferably present at levels of 0.001% and 10% or even 0.01 to 5% or even 0.05 to 1% by weight of the component. It may be preferred that the foam component contains an acidic material and/or an alkaline material and/ or buffering agent. This may be the polymeric material and/ or the active ingredient, or an additional ingredient. It has been found that in particular the presence of an acidic material improves the dissolution and or dispersion of the foam component of the invention upon contact with water, and can also reduce or prevent interactions, leading to for example precipitation, of the polymeric material in the foam component with cationic species present in the aqueous medium. It may also be preferred to include a preservative ingredient in the foam component to prevent microbial contamination or growth. Examples may include formaldehyde and formaldehyde releasing materials any other known preservative material. Liquid The liquid herein is preferably a solvent for the polymeric material and/ or the active material. Preferably the solvent comprises at least water. Also preferred are also organic solvents such as alkanes, alkenes, alcohols, aromatic solvents such as benzene, phenol, or mixtures thereof. Polymeric Material Any polymeric material which can be formed into a air-stable, water-unstable foam, can be used in the foam component and can be used to form the matrix or part thereof, of the foam component. Preferred it that the polymeric material comprises a water-dispersible or more preferably a water-soluble polymer. Preferred water-dispersable polymers herein have a dispersability of at least 50%, preferably at least 75% or even at least 95%, as measured by the method set out hereinafter using a glass-filter with a maximum pore size of 50 microns; more preferably the polymer herein is a water-soluble polymer which has a solubility of at least 50%, preferably at least 75% or even at least 95%, as measured by the method set out hereinafter using a glass-filter with a maximum pore size of 20 microns, namely: Gravimetric method for determining water-solubility or water-dispersability of polymers: 50 grams ± 0.1 gram of polymer is added in a 400 ml beaker, whereof the weight has been determined, and 245ml ± 1ml of distilled water is added. This is stirred vigorously on magnetic stirrer set at 600 rpm, for 30 minutes. Then, the water-polymer mixture is filtered through a folded qualitative sintered-glass filter with the pore sizes as defined above (max. 20 or 50 microns). The water is dried off from the collected filtrate by any conventional method, and the weight of the remaining polymer is determined (which is the dissolved or dispersed fraction). Then, the % solubility or dispersability can be calculated. Preferred are polymers selected from polyvinyl alcohols, polyvinyl pyrrolidone, polyalkylene oxides, cellulsoe ethers, polycarboxylic acids and salts, polyaminoacids or peptides, polyamides, polyacrylamide, or derivatives or copolymers thereof. More preferably the polymer is selected from polyvinyl alcohols or derivatives thereof, cellulose ethers derivatives, including hydroxypropyl methylcellulose, copolymers of maleic/acrylic acids or mixtures thereof. Most preferred is that the polymeric material comprises or consists of polyvinyl alcohol and/ or derivative thereof. Copolymers, block polymers and graft polymers of the above can also be used. Mixtures of polymers can also be used. This may in particular be beneficial to control the mechanical and/or dissolution properties of the foam component, depending on the application thereof and the required needs. The polymer can have any average molecular weight, preferably from about 1000 to 1,000,000, or even from 4000 to 250,000 or even from 10,000 to 200,000 or even from 20,000 to 75,000. Preferred can be that the polymer used in the foam component herein has a secondary function when dissolved in water, for example when the foam component comprises ingredients of cleaning products, it may be useful that the polymeric material comprises a polymer which is a builder polymer, soil release polymer, dye transfer inhibiting polymer, process aid, suds suppressor, dispersant, flocculant etc. Active Ingredient The active ingredient can be any material which is to be delivered to an aqueous environment and is active in an aqueous environment, e.g. which performs in water or upon contact with water. For example, when used in cleaning compositions the foam component can contain any active cleaning ingredients. Highly preferred ingredients are hazardous materials, agrochemicals, drugs or medicines, cleaning actives. The active ingredient may be a mixture of materials, for example, a complete product formulation may be incorporated in the foam component. For example, when used in cleaning compositions the active ingredient may be a complete cleaning product formulation, comprising preferably at least builder and surfactant, preferably also enzymes and perfume, preferably also chelating agent, bleach, brightners, sudsuppressers. In particular, it is beneficial to incorporate in the foam component active ingredients which are temperature-sensitive (unstable, reactive under increased or reduced heat), volatile, moisture sensitive (react upon contact with moisture), or solid ingredients which have a limited impact robustness and tend to form dust during handling. In particular preferred in foam components are active ingredients such as enzymes, perfumes, bleaches, bleach activators, fabric softeners, fabric and hair conditioners, dyes, colourants, surfactants, such as liquid nonionic surfactant, conditioners, antibacterial agents, effervescence sources, brighteners, photo-bleaches and mixtures thereof. Preferred are anionic surfactants, which include soaps salts (including, for example, sodium, potassium, ammonium, and substituted ammonium salts such as mono-, di- and triethanolamine salts) of the anionic sulfate, sulfonate, carboxylate and sarcosinate surfactant, preferabaly linear or branched alkyl benzene sulfonate, alkyl sulphates and alkyl ethoxylsulfates, isethionates, N-acyl taurates, fatty acid amides of methyl tauride, alkyl succinates and sulfosuccinates, monoesters of sulfosuccinate (especially saturated and unsaturated C , -C, ^ monoesters) diesters of sulfosuccinate (especially saturated and unsaturated C^-C, . diesters), N-acyl sarcosinates. Also preferred are nonionic surfactants such as nonionic surfactant, preferably selected from the classes of the nonionic condensates of alkyl phenols, nonionic ethoxylated alcohols, nonionic ethoxylated/propoxylated fatty alcohols, nonionic ethoxylate/propoxylate condensates with propylene glycol, and the nonionic ethoxylate condensation products with propylene oxide/ethylene diamine adducts. Cationic surfactants and softening agents may also be included as active ingredient in the foam component herein, for example to quaternary ammonium surfactants and softening agents, and choline ester surfactants,. Perfumes or perfume compositions are highly preferred active ingredients in the foam component. Another active ingredient is hydrogen peroxide and/ or perhydrate bleach, such as salts of perborates, salts of percarbonates, particularly the sodium salts. Also preferred active ingredients are organic peroxyacid bleach precursor or activator compound, preferred are alkyl percarboxylic precursor compounds of the imide type include the N-,N,Nl]S.l tetra acetylated alkylene diamines wherein the alkylene group contains from 1 to 6 carbon atoms, particularly those compounds in which the alkylene group contains 1, 2 and 6 carbon atoms such as tetraacetyl ethylene diamine (TAED), sodium 3,5,5-tri-methyl hexanoyloxybenzene sulfonate (iso-NOBS), sodium nonanoyloxybenzene sulfonate (NOBS), sodium acetoxybenzene sulfonate (ABS) and pentaacetyl glucose, but also amide substituted alkyl peroxyacid precursor compounds Highly preferred active ingredient for use in the foam component herein are one or more enzymes. Preferred enzymes include the commercially available lipases, cutinases, amylases, neutral and alkaline proteases, cellulases, endolases, esterases, pectinases, lactases and peroxidases conventionally incorporated into detergent compositions. Suitable enzymes are discussed in US Patents 3,519,570 and 3,533,139. Preferred commercially available protease enzymes include those sold under the tradenames Alcalase, Savinase, Primase, Durazym, and Esperase by Novo Industries A/S (Denmark), those sold under the tradename Maxatase, Maxacal and Maxapem by Gist-Brocades, those sold by Genencor International, and those sold under the tradename Opticlean and Optimase by Solvay Enzymes. Preferred amylases include, for example, α-amylases obtained from a special strain of B licheniformis, described in more detail in GB- 1,269,839 (Novo). Preferred commercially available amylases include for example, those sold under the tradename Rapidase by Gist-Brocades, and those sold under the tradename Termamyl, Duramyl and BAN by Novo Industries A/S. Highly preferred amylase enzymes maybe those described in PCT/ US 9703635, and in WO95/26397 and WO96/23873. The lipase may be fungal or bacterial in origin being obtained, for example, from a lipase producing strain of Humicola sp., Thermomyces sp. or Pseudomonas sp. including Pseudomonas pseudoalcaligenes or Pseudomas fluorescens. Lipase from chemically or genetically modified mutants of these strains are also useful herein. A preferred lipase is derived from Pseudomonas pseudoalcaligenes. which is described in Granted European Patent, EP-B-0218272. Another preferred lipase herein is obtained by cloning the gene from Humicola lanuginosa and expressing the gene in Aspergillus orvza. as host, as described in European Patent Application, EP-A-0258 068, which is commercially available from Novo Industri A/S, Bagsvaerd, Denmark, under the trade name Lipolase. This lipase is also described in U.S. Patent 4,810,414, Huge- Jensen et al, issued March 7, 1989. In personal-care foam components, it may be highly preferred that the active material includes cationic organic compounds, such as cationic surfactants, ingredient which can reduce dermatitis or compounds which can help the healing of the skin, metal-containing compounds, in particular zinc-containing compounds, vitamins and cortisone' s, and also compounds to soften the skin such as vaseline, lanolin, and other actives typically employed by pharmaceutical and cosmetic manufactures. Complete product compositions may also be included as preferred active ingredients, such as commercially available cleaning products, pharmaceutical products, personal- care products, cosmetic products and fabric-care products. Form of Foam Component The foam component can be made into any form, by any conventional method. Preferred may be that the foam component is in the form of granules, beads or tablets, or a rod or a sheet. Preferred may also be that the foam component is shaped in a rod or sheet and then subsequently formed into any object shape or geometric shape such as sphere, ball, cube, or letters or animal shape for a children's product, what ever is desirable for the user. These shapes may also be formed directly, without the intermediate formation of a foam rod or sheet. The granules can be made by shaping the mixture under pressure through a die or for example through an extruder and subsequently reducing the size of the extruded rod into the required granule size. Preferred granules have a weight average particle size of from 10 to 2000 microns, more preferably from 50 to 2000, even more preferably from 100 to 1500 microns or even form 200 to 1000 microns. The foam component may also be in the form of a sheet, which can have any dimension and can be subsequently reduced in size as required. It may be preferred that the sheet has a mean thickness of from of from 0.01 microns to 10 centimeters, more preferably from 0.05 microns to 5 centimeters, or even more preferably from 0.1 microns to 3 centimeters. It may be preferred that the foam component is in such a form, preferably a sheet form, that it can be used to encapsulate or coat a product. Preferred may be that the foam component forms a pouch structure around the product. For example, the foam component can be used to encapsulate a cleaning product, fabric care product, personal care product, cosmetic product or pharmaceutical product. Such an encapsulate or pouch can for example conveniently be made by heat sealing a sheet of the foam component around the product. The foam component may also be an absorbent article or comprised in an absorbent article such as a feminine protection article, or diaper, or an article to cover the skin to release the actives in the to the skin whereto the absorbing articles is applied, when in contact with water, such as body fluids, for example diapers, wipes, catamenials, plaster, bandages. The foam component may also be incorporated in any compositions which requires active ingredients to be protected against moisture during storage, against chemical reactions with other ingredients, migration or phase separation of ingredients, or protection against physical forces. In particular, the foam component is useful in cleaning compositions, fabric care compositions, personal care compositions, cosmetic compositions, pharmaceutical compositions. These compositions may be solid or liquid. They may comprise any additional ingredients, including additional amounts of the active ingredients or polymeric material described above. Preferred are laundry and dish washing detergent compositions and fabric conditioners and other rinse aids. The cleaning compositions typically contain one or more components selected from surfactants, effervescence sources, bleach catalysts, chelating agents, bleach stabilisers, alkalinity systems, builders, phosphate-containing builders, organic polymeric compounds, enzymes, suds suppressors, lime soap, dispersants, soil suspension and anti-redeposition agents, soil releasing agents, perfumes, dyes, dyed speckles, brighteners, photobleaching agents and additional corrosion inhibitors. For laundry detergent compositions and fabric care compositions it may be preferred that the component preferably comprise at least one or more softening agents, such as quaternary ammonium compounds and/ or softening clays, and preferably additional agent such as anti-wrinkling aids, perfumes, chelants, fabric integrity polymers. Processing example An APN lab extruder (model MP19CH) was used to make the following water-soluble foam component. A viscous mixture of 1600gr water, 613gr glycerine (Sigma/ Aldrich 13487-2) and lOOOgr Lineair alkyl benzene sulphonate sodium salt (LAS) surfactant paste (76% active) was made using an overhead stirrer. Powdered polyvinyl alcohol (Sigma/ Aldrich P8136) (1900gr) was added to the extruder via the powder feed, and the viscous mixture was added slightly downstream of the powder via an injection system on a side entry port. Air was added with the liquid (by aerating with a Kenwood-type food mixer), at a volume ratio of 3 parts air to 1 part viscous mixture. The viscous mixture feed was run at a constant rate of about 100 gr/min, and the powder PNA feed about 60 gr/min. Screw speed of the extruder was 400 RPM. The last 4 sections of the extruder barrel were heated to 65°C. Pressure just before the extruder exit was approximately 25bar. The approximate viscosity of the viscous mixture comprising the PNA powder (in the extruder; without air incorporation) was 200Pa.s at 1.7s "1 The foam component produced at the extruder outlet was collected this was further shaped by and adding it in petri-dish moulds to give a series of foam discs, which were allowed to dry in ambient conditions. This drying was complete in <2 hours, giving a dry foam that was water-soluble, air-stable, elastic, and could be easily handled. The dry foam had a density of approx. 0.24g/cm3 and a remaining water content of approx. 5% by weight. This experiment was repeated with (replacing the lOOOgr LAS paste): - 1000 gr enzyme (protease, lipase, amylase, cellulase or mixtures thereof); - lOOOgr of a mixture of (weight %) 30% LAS, 20% perfume oil, 20% soap, 10% bleach, 20%) cationic surfactant; - 1000 gr of a mixture of (weight %) 80% betaine surfactant, amphoteric surfactant, cationic surfactant, anionic surfactant and/ or nonionic surfactant (70% active paste of one or more of these surfactants) and 20% perfume oil; - lOOOgr of a 70% active paste of cationic fabric softening agent or cationic hair conditioner; - lOOOgr of a mixture of (by weight) 40% sodium percarbonate 30% activator, 30% surfactant.

Claims: What is claimed is: 1. A process for making a foam component comprising a polymer matrix and an active material, which is active in water, the foam component being unstable upon contact with water and stable upon contact with air, the process involving: a) obtaining a viscous mixture of a polymeric material and an active material having a viscosity of at least 150 Pa.s at a shear rate of 1.7s "1 and/ or obtaining a viscous mixture and intensively mixing said mixture with a power/mass of at least 20W/gr, preferably at least 3 OW/gr; b) introducing a gas or agent which forms a gas (at 25 °C and atmospheric pressure); c) pressurising the mixture of b) with a pressure of at least 2 bar; and d) shaping the mixture of c) and releasing the pressure to obtain the foam component. 2. Process of claim 1 whereby the mixture comprises a liquid, preferably a solvent for the polymeric material and/ or the active material, and whereby in step d) the liquid or part thereof is evaporated, preferably at least by the release of pressure. 3. Process according to claim 1 or 2 whereby at least step c) is done in an extruder, preferably steps a), b) and c) are done in an extruder. 4. Process according to any preceding claim whereby in addition to the gas introduced by mixing, an additional gas or agent is physically or chemically introduced in the mixture. 5. A process according to any preceding claim whereby the mixture in step a) comprises up to 40% by weight of a liquid, preferably up to 35% by weight, and at least 10% by weight of active material, preferably at least 20% by weight and preferably a plasticiser. 6. A process according to any of claims 2 to 5, whereby the evaporation of the liquid or part thereof is further aided by heating the component up to a temperature up to 70°C, preferably up to 55°C. 7. A process as in any preceding of claims 2 to 6 whereby in step a) and b) the temperature of the mixture is below the melting point of the polymeric material and . whereby preferably the mixture is heated up to a temperature below the boiling point of the liquid. 8. A process according to any of claims 2 to 7 whereby the liquid comprises water and the polymeric material is water-soluble. 9. A process according to any preceding claim whereby the polymeric material comprises polyvinyl alcohol polymer and/ or derivative thereof. 10. A process according to any preceding claim whereby the active material comprises a temperature-sensitive active ingredient, preferably a heat-sensitive or volatile ingredient. 11. A foam component obtainable by a process according to any preceding claim, preferably being such that it partially or completely dissolves upon contact with water. 12. A foam component according to claim 11 , in the form of a granule or article, said granule typically having an average diameter of 10-2000 microns and the article typically having at least one dimension of a size of more than 2000 microns, preferably being a geometric object, including a sheet, cube, sphere. 13. A foam component according to claim 11 or 12 whereby the active material comprises a cleaning product ingredient, fabric care ingredient, pharmaceutical ingredient, cosmetic ingredient, personal care ingredient, preferably at a temperature-sensitive active ingredient, preferably a heat-sensitive or volatile ingredient. 14. A foam component according to claim 14 whereby the active material comprises an enzyme, perfume, bleaching agent or mixture thereof. 15. A flexible foam component according to any of claims 11 to 14 which has an elastic modulus of less than 10 GN.m "2 , preferably less than 1 GN.m "2 . 16. A foam component according to any of claims 11 to 15 which has a relative density of 0.05 to 0.9. 17. A foam component according to any of claims 11 to 16 comprising a plasticiser, preferably selected from glycerol, ethylene glycol, diethyleneglycol, propylene glycol, sorbitol.

Inventors: DUFTON DANIEL JAMES, DUFTON, DANIEL, JAMES
Applicants: PROCTER & GAMBLE, THE PROCTER & GAMBLE COMPANY
Application year: 2001
Main classification: C11D3
IPC codes: A61K8, A61Q5, B29C44, B29C47, B29K29, B29K105, C08J9, C11D3, C11D11