GB2361928A

GB2361928A - Elastic packaging or binder material

Info

Publication number: GB2361928A
Application number: GB0010599A
Authority: GB
Inventors: Scott Edward Stephans; Andrew Edward Bayly; Didier Marcel Corrand; Matthew Grady Mcgoff; Hossam Tantawy; Christopher Charles Driffield
Original assignee: Procter and Gamble Co
Current assignee: Procter and Gamble Co
Priority date: 2000-05-03
Filing date: 2000-05-03
Publication date: 2001-11-07
Also published as: GB0010599D0

Abstract

The present invention relates to elastic articles comprising a polymeric matrix and an active ingredient, such as detergent ingredients, typically to be delivered to aqueous environment. Highly preferred active ingredients include enzymes. A preferred elastic article is a foam which is stable upon contact with air but dissolves, disintegrates or disperses in water. The invention also relates to compositions containing the articles and methods for making the articles. The elastic articles are characterised by the nature of the matrix of the coating composition which has a glass transition temperature (Tg) less than 50{c, as well as being in a homogenous mixture with the active the matrix may be a coating phase.

Description

2361928 Elastic articles and uses thereof Technical Field The present

invention relates to elastic articles, typically beads. particles or tablets, comprising a matrix of a polymeric material, a plasticiser and/ or water and an active ingredient, such as detergent ingredients, typically to be delivered to an aqueous environment. The invention also relates to compositions containing the elastic articles and methods for making the elastic articles.

Background to the Invention

Compositions such as cleaning products and personal-care products, cosmetics and pharmaceuticals, often comprise active ingredients which are to be delivered to water or which are required to be active in aqueous conditions, but which are sensitive to moisture, temperature changes, light andlor air during storage. Also, these compositions often contain ingredients which may react with one another. Therefore, such ingredient or actives are often protected or separated from one another by coating agents or encapsulating agents. For example enzymes, used in detergents, are often incompatible with alkaline or acid materials, bleaches, moisture and light and thus coated to protect them. Because the active materials generally need to be delivered in aqueous conditions, the coating materials need to be chosen such that the coating and actives dissolve or disperse weft in water.

Another problem with many solid ingredients, in particular enzymes, is that they tend to form dust during handling due to physical forces. This not only creates waste product, but the dust can also cause hygiene and health problems. Again, coating of the ingredients can improve this problem to some extent. The problem with many coated particles is that they do not always exhibit sufficient impact resistance during 2 handling. Thus, even when handling encapsulated enzyme particles, dust is formed which causes health and hygiene problems. One proposed solution to reduce dust formation is to make these granules harder.

The inventors have now found an improved method of protecting actives and delivering actives to liquid environments such as aqueous envirorunents. They found that specific elastic articles having a matrix, for example a core or coating, made ftorn polymeric material having a specific glass transition temperature, are very impact robust and the active ingredient incorporated in such an article are effectively protected, not only against air-moisture and chemical reactions but also against physical forces. Thus, the resulting elastic articles have been found to be very impact resistant, thus resulting in reduced braking-up or abrasion during handling and reduced dust formation. For example, elastic particles or beads with enzymes can thus be obtained which are safer and more efficient to handle. Moreover, these articles can be made such that they still deliver the actives very efficiently to liquid, e.g.aqueous, environments. Preferably the article is in the form of a foam article, which is air-stable under normal humidity storage conditions, but unstable upon contact with water, to thus deliver the actives.

The elastic article is useful in any product, in particular useful in cleaning products, pharmaceutical products, personal-care products, cosmetic products and fabric-care products.

Sumni@jy of the Invention The invention relates to an elastic article comprising a) an active ingredient; b) a matrix formed ftom a polymeric material and a plasticiser, provided that when the plasticiser consist of water, the level of water is at least 3% by weight of the article (based on free- moisture level), whereby the article is capable of delivering the active to a liquid environment, and whereby the matrix has a glass transition temperature (Tg) below WC, preferably 3 below 40'C, and whereby the active ingredient may be present in the matrix, or may be outside the matrix Preferably the matrix has a Tg of less than 20'C or even from -20'C or even -10'C to 1 O'C or even to O'C, and preferably the matrix has such an elasticity that it has an elastic modulus of less than 1 GN. m -2, preferably less than 0. 5 or even 0. 1 GNM-2.

It may thus be preferred that the active ingredient is present in the matrix, for example that the polymer material and active ingredient are homogeneously mixed within the matrix, or for example, it may be preferred that the matrix is in the form of a coating or layer around the active ingredient.

The elastic article preferably releases the active ingredient or part thereof upon contact with water, the article and the matrix preferably partially or completely disintegrating, dispersing, denaturing and/ or dissolving upon contact with water.

The elastic article is preferable an elastic foam article. The elastic article may preferably be in the form of particles or beads.

Preferably the active ingredients are cleaning actives, personal-care or cosmetic actives or pharmaceutical actives. The elastic article may also contain mixtures of active ingredients, which may be particularly useful to improve the storing of active ingredients which can react with one another. By use of the elastic article, it can be achieved that such ingredients only become active once released into the aqueous conditions. The article may comprise full compositions, or only some or one active ingredients to be incorporated in such compositions.

The invention also relates to processes for making the elastic article, and compositions comprising the elastic article.

4 The invention also relates to the use of elastic arlicles according to the invention to deliver active ingredients to an aqueous environment, preferably the active ingredients being detergent active ingredients and the aqueous environment being the wash water. The elastic article can be such that delayed release of the active ingredient to the aqueous environment can be achieved. The invention also relates to the use of an elastic article according to the invention to incorporate enzymes in compositions, preferably detergent compositions.

Detailed Descriptio

Elastic article and matrix thereof The elastic article of the invention comprises a matrix comprising, and formed from, a polymeric material and a plasticiser and optionally other materials. The matrix may comprise the active ingredient, or part thereof, or the active ingredient may be present outside the matrix, for example enclosed by the matrix ( the matrix coating or encapsulating the active ingredient). Thus, the polymer material and the active ingredient may be intimately nfixed or even homogeneously nfixed, in which case a socalled monophase elastic article is obtained, which has uniform physical and chemical properties. However, it may be preferred that the active ingredient and the polymeric material are present in the matrix in a non-homogeneous form, forming a multiphase elastic article, whereby on a microstructure level one or more of the active ingredients is present in lower or higher amounts in one area of the matrix than in an other area of the component, and thus lower or higher than the average obtained by intimate ini)mg.

It may also be preferred that the active ingredient is present in the core or an inner shell or layer of the article, enclosed by the matrix. It may also be preferred that part of the matrix forms a core or inner shell or layer of the article, which is then enclosed by a layer of the active ingredient and then preferably by another layer of the matrix material.

The elastic article comprises preferably at least 1 % by weight of the active ingredients, more preferably from 5% to 70%, more preferably at least 10% by weight of the matrix, more preferably from 15% or even 20% or even 25% to 50%.

The elastic article comprises preferably from 10% to 99% by weight of the matrix, more preferably at least 20% or even 30% to 99%, more preferably from 20% or 30% to 90% to 80% by weight. The plasticiser may consist of water, provided that it is then present at a level of at 10 least 3% by weight of the article (based on ftee-moisture level). Preferably, at least a plasticiser other than water is present, as described below in more detail. Essential to the invention is that the matrix has a glass transition temperature Tg, as defined below, of less than 50T, preferably less than 40T preferably less than 2WC 15 or even less than 1 OIC or even less than O'C. Preferably the glass transition temperature is above -20'C or even above -10'C. The Tg of the matrix when used herein, is the Tg of the polymeric matrix as present in the article, which thus may be a mixture of polymeric material and plasticiser alone, or 20 a mixture of polymeric material, plasticiser and active ingredient, and in either case, optional additional ingredients may be present (such as stabilisers, densification aids, fillers, lubricants etc., as described herein). The glass transition temperature as used herein is as defined text book 'Dynan-fic 25 Mechanical Analysis' (page 53, figure 3. 11 c on page 5 7), being the temperature of a material (matrix) where the material (matrix) changes from glassy to rubbery, namely where chains gain enough mobility to slide by each other. The Tg of the matrix of the article of the invention can be measured in the Perkin30 Elmer DMA 7e equipment, following the directions in operations manual for this 6 equipment, generating a curve as illustrated in the book Dynamic Mechanical Analysis - page 5 7, figure 3 -11 c. The Tg is the temperature or log Frequency as measured with this equipment, between the glass and 'leathery region', as defined in that text.

The matrix, and preferably the elastic article as a whole, has a specific elasticity and flexibility, because of its specific glass transition temperature. In particular, this means that the matrix and the article reversibly deform, absorbing the energy of impacts or of forces so that the article or matrix remains substantially its original bulk volume after the physical force seizes to be applied on the component.

The elasticity can be defined by the elastic modulus of the matrix, or even the article, which again can be defined by the Young's modulus. This can be calculated from strain or stress mechanical tests as known in the art, for example by using PerkinElmer DMA 7e equipment following the manufacturer's experimental procedure over a specific % static strain range, namely in the range of 10-40% static strain. This represents a maximum strain as could be applicable during normal manufactering or handling. Thus, the elastic modulus as defined herein is the maximum modulus as measured with this equipment in the range of 10% to 40% static strain. For example a piece of matrix (or article) of I CM3 can be used in the testing with this equipment.

The matrix herein typically has an elastic modulus or Young's modulus of less than 4 2 GN.m-2, or typically less than 2 GN.m-2, even more preferentially less than I GN.m", but typically even less than 0. 5 GN. m"2, or even less than 0. 1 GN. m-2, or even less than 0. 0 1 GN. fff2, as measured with the Perkin-Elmer DMA 7e equipment. In particular a matrix herein which contains gas bubbles, e.g. formed by processes involving the introduction of air in the matrix, has an elastic modulus below 0. 1

GN. M-2 or even 0. 0 1 GN. in -2 or even below 0.005 GN. M-2 or even below 0. 000 1 GN.rn-2.

Preferably the matrix is flexible, such that it has a relative yield strain greater than 2%, and preferably greater than 15% or even greater than 50%, as measured with the 7 Perkin-Elmer DMA 7e equipment. (The vield strain is in this measurement the limit deformation of a piece of matrix at which the it deforms irreversible).

In particular this means that when a matrix sample having a cross section of a specific length, for example I cm, 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 matrix is preferably flexible to such an extend that when a matrix sample having a cross section of a specific length, for example lem, 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 I 10% of the original length. This can for example be measured by use of Perkin-Elmer DMA 7e equipment.

In particular, when using this equipment, the static forces applied along the axis of a cross section of a I CM3 matrix sample are graduafly 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 matrix sample in the direction of the cross section is measured. Preferably, this length of the cross section after this experiment is preferably from 90% to I 10% of the original length of the cross section, preferably from 95% to 105% or even from 98% to 100%.

The elastic modulus or Young's modulus is related to the relative density, namely 2 E P Es ('OS.), where p is the relative density of the matrix or even the article, and p,, is the relative densities of the components of the matrix or article, as described herein, and E is the 8 Young's modulus of the matrix or even the elastic article itself, and E, that of the components of the matrix or even the article This means that even a stiff polymeric material, with a high E, can be made into an elastic, flexible matrix by adjusting the levels and/ or type of plasticiser and optionally by modifing the density (or for example by introducing gas during the making process to form elastic foam articles, as described below).

The elastic article of he invention is typically used to deliver actives to aqueous environment. Then, the elastic article, and preferably the matrix thereof, is unstable when brought into contact with water. This occurs such that the active ingredients or part thereof, present in the article is delivered to the water. Preferably the article 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 elastic article is such that the polymeric material of the matrix of the article disperses or dissolves - preferably at least 10% of the polymeric material, by weight, is dissolved or rapidly. dispersed in 30 minutes after contacting the article with water, or 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 elastic article 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 elastic article is such that the total volume of the article is changed, preferably reduced, with at least 10%, compared to the initial total volume, as for example can be determined when 1 cm' of the article is added to 100 ml of deminerafised water upon and stirred for 5 minutes at a speed of 20Orpm, 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 article is disintegrated, dispersed or preferably dissolved into the water quickly.

9 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' of an elastic article is obtained and introduced in a 100 mI micro volumetric 5 measuring cylinder which is filled with 50 mI 0. Imi 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 matrix of the elastic article herein, for example when this is PVA. Other neutral organic medium can be used according to the nature of the article under investigation; the inert solvent is such that the article 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 elastic article. The change in volume is measured and taken as the original volume Vi of the foam specimen. The article is then removed from the solvent and left to dry in air so that the solvent evaporates.

The article is then placed in a 250 mi beaker containing 100 rnI of demineralised water, maintained at 250C, under stirring at 200 rpm with the help of a magnetic stirrer, for 5 minutes. The remaining of the article specimen, if any, is filtered off with a 60mm mesh copper filter and placed in an oven at a temperature and for a period such that residual water is removed. The dried remaining article 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 elastic article Vf.. The decrease in total volume AV of the elastic article specimen is then:

%AV= 9f 100 vi The matrix of the elastic article, or possibly even the article as a whole, has preferably a relative density p 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 form 0.3 to 0.7. The relative density is the ratio of the density of the matrix or the article (p), to the sum of the partial densities of all the bulk materials used to form the matrix, or the article (p,).

The matrix or even the article as a whole, is preferably in the form of a foam and 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.

Preferably, the ratio of the closed cells to open cells in the matrix of the article, or the article as a whole is more than 1: 1, preferably more than 3:2 or even more than 2.1 or even more than 3: 1. This ratio can be determined by calculating the Total Volume of a specimen of the matrix or article, VT, (assuming a spherical shape), and then measuring with a Mercury Porosimetry Test method the Open Cell Volume(Vo) and subtracting the Open Cell Volume from the Total Volume should deliver the Closed Cell Volume (Vc.. VT VO + W.) The preferred foamed article or foamed matrix, as used herein, is typically air-stable or stable upon contact with air, which means herein that the bulk volume of the article or matrix thereof substantially remains the same when exposed to air. This means in particular that the article or matrix thereof 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 = 25T) for 24 hours. Preferably the elastic article or the matrix thereof, 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 calibrated image analyser software. A 1 cm 3 specimen of the article or the matrix thereof is obtained and introduced in an open beaker having a diameter of 9 cm and stored for 24 hours at the abo,,,e 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 5 bulk volume change is calculated in %.

Preferably, the elastic article or matrix thereof is such that, when in the form of particles of a mean particle size of 2000 microns or less, these 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 such 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 elastic particles re-arrange themselves in a stable position with a horizontal top surface. The volume is measured. The open beaker with the elastic particles is then carefully placed in the incubator for 24 hours, set to the desired 'YoRH and temperature. The bulk volume after the 24 hours is measured and the change of bulk volume is calculated in PolMneric Material and Plasticiser Any polymeric material can be used to form the matrix herein, provided it has itself a Tg as defined above or more typically, it can be formed into a matrix of the Tg as defined above by using a suitable amount of plasticiser.

Preferably, the polymer material comprises or consists of amorphous polymer(s).

The polymeric material may consist of a single type of homologous polymer or may be a mixture of polymers. Mixtures of polymers may in particular be beneficial to control the mechanical and/or dissolution properties of the elastic article, depending on the application thereof and the requirements thereof 12 Preferred it that the polymeric material comprises a water-dispersible or more preferabl- a vater-sohuble pollymer 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 glassfilter with a maximum pore size of 20 microns, namely:

Gravimetric method for determining water-solubifity or waterdispersability of polymers: 50 grams 0. 1 gram of polymer is added in a 400 H beaker, whereof the weight has been determined, and 245ml I in] of distilled water is added. This is stirred vigorously on magnetic stirrer set at 600 rpm, for 30 minutes. Then, the waterpolymer 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 ftom 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 and derivatives thereof, polyethylene glycols and derivatives thereof, polyvinyl pyrrolidone and derivatives thereof, cellulose ethers and derivatives thereof, and copolymers of these polymers with one another or with other monomers or oligomers. Most preferred are PVP (and derivatives thereof) and/ or PEG (and derivatives thereof) and most preferably PVA (and derivatives thereof) or mixtures of PVA with PEG and/ or PVP (or derivatives thereof). Most preferred may also be a polymeric material only comprising PVA.

Preferably, such polymers have a level of hydrolysis of at least 50%, more preferably at least 70% or even from 85% to 95%.

13 The polymer can have any a,,.-eraú-)e f-rom 1000 to 1,000,000, or even form 4000 to 250,000 or even form 10,000 to 200,000 or even form 20,000 to 75,000. Highly preferred may be polymeric material having a weight average molecular weight of from 30,000 to 70,000.

Cross-linking agents may be added to modify the properties of the matrix and the resulting article as appropriate. Borate may be useful in the matrix.

Depending on the required properties of the article, the polymer material can be adjusted. For example, to reduce the solubility, polymers may be included in the material, which have high molecular weights typically above 50,000 or even above 100,000, and vise versa. For example, to change the solubility, polymers of varying level of hydrolyses may be used. For example, to improve (reduce) the elastic modulus, the cross-linking of the polymers may be increased and/ or the molecular weight may be increased.

It may be preferred that the polymer used in the elastic article herein has a secondary function, for example a function in the composition wherein article is to be incorporated. Thus for example for cleaning products, it is useful when the polymer in the polymeric material is a dye transfer inhibiting polymer, dispersant etc.

Any plasticiser which is suitable to aid the formation of a matrix as defined herein can be used. Nfixtures of plasticiser may also be used. Preferably, when water is used, an additional plasticiser is present.

Preferably, the plasticiser or at least one of the plasticisers, has a boding point above 40Q preferably above WC, or even above WC, or even above 120'C, or even above 150'C.

14 Preferred plasticisers include glycerol or glycerine, glycol derivatives including ethylene LIvcol. digomeric polvetfiviene glycols such as diethdene tri 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, su gars, 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 The plasticiser is preferably present at a level of at least 0.5% by weight of the article, preferably by weight of the matrix, provided that when water is the only plasticiser it is present at a level of at least 3% by weight of the article, or preferably by weight of the matrix.

Preferably, the plasticiser is present at a level of 1 % to 3 5% by weight of the article or matrix, more preferably 2% to 25% or even to 15% or even to 10% or even to 8% by weight of the article or by weight of the matrix. The exact level will depend on the polymeric material and plasticiser used, but should be such that the matrix of the article has the desired Tg. For example, when urea is used, the level is preferably 1 % to 10% by weight of the matrix, while when glycerine or ethylene glycol or other glycol derivatives are used, higher levels may be preferred, for example 2% to 15% by weight of the article or matrix.

The ratio of plasticiser to polymeric material in the matrix is! to more preferably 1 to 70 or 1 to 50, more preferably 1 to 30 or even 1 to 20, again depending on he type of plasticiser and polymeric material used. For example, when the polymeric material comprises PVA and the plasiciser comprises glycerine or glycerol derivatives and optionally water, the ratio is preferably around 1 - 15 to 1: 8, a preferred ratio being around 10: 1.

Active Ingedient The active ingredient can be any material which is to be delivered to a liquid environment, or preferably an aqueous environment and preferably an ingredient which is active in an aqueous environment. For example, when used in cleaning compositions the article can contain any active cleaning ingredients. The articles may also comprise compositions, such as cleaning composition or personal care compositions.

In particular, it is beneficial to incorporate in the elastic article active ingredients which are moisture sensitive or 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 elastic articles are active ingredients, such as enzymes, perfumes, bleaches, bleach activators, fabric softeners, fabric conditioners, surfactants,such as liquid nonionic surfactant, conditioners, antibacterial agents, effervescence sources, brighteners, photo-bleaches and mixtures thereof Another active ingredient is a perhydrate bleach, such as metal perborates, metal 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,N IN I 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 16 carbon atoms such as tetraacetyl ethylene diamIne (TAED), sodium 3.55-trl- methyl hexanoyloxybenzene sulforiate (iso-NNOBS), sodium nonanovloxvbenzene SI-11',onate (NOBS), sodium acetoxybenzene sulfonate (ABS) and pentaacetyl glucose, but also amide substituted alkyl peroxyacid precursor compounds 5 Highly preferred active ingredient for use in the elastic article 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 15 tradename Opticlean and Optimase by Solvay Enzymes. Preferred amylases include, for example, oc- 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 20 A/S, IFfighly preferred amylase enzymes maybe those described in PCT/ US 9703635, and in W095/26397 and W096/23873. The hpase may be fungal or bacterial in origin being obtained, for example, from a lipase producing strain of Humicol sp., ThermoMyces sp. or Pseudomonas sp. including Pseudomonas pseudoalcaligenes or Pseudomas fluorescens. Lipase from chemically or genetically 25 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 lanuginos and expressing the gene in Aspergillus o, as host, as described in 30 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 17 is also described in U. S. Patent 4,810,414, Huge-Jensen et al, issued March 7, 1989.

Processes for makinp ---the elastic article The elastic article of the invention can be made by any process of making a polymer matrix of the defined Tg from a polymeric material and a plasticiser, and combining an active ingredient with such a matrix- Preferred processes involve chemically or physically introducing a gas in a mixture of the polymeric material and plasticiser and optionally the active ingredient.

A preferred process for making the article herein comprising the step of a) obtaining a mixture of a polymeric material and a plasticiser, preferably water and an additional plasticiser.

b) chemically or physically introducing gas in said mixture of polymeric material and water.

c) prior to step b) and/or simultaneously with step b) and/ or subsequently to step b), addition of the active ingredient to the mixture of polymer material and water; d) shaping of articles of the resulting mixture of step c); whereby one or more of steps a) to d) are foIlowed or accompanied by removal of part of the water, if present.

Step c) preferably comprises the step of obtaining a body comprising the active ingredient or part thereof and enclosing said body with the mixture of step b).

In step a) the mixture is preferably an aqueous mixture or slurry and after or in step b), c) and/ or d), part of the water is removed such that the resulting article comprises 3% by weight of free-moisture, or more.

Preferably, the article comprises open and/ or closed cells and the process comprising 30 the steps of 18 a) formation of a mixture of the polymeric material, the active material, a plasticiser and a liquid, whereby the liquid and the plasticiser may be the same compound., b) shaping of bodies from the mixture of claim b) and b) evaporation of the liquid or part thereof to form spacings in the mixture which form the inner area of the cells of the article, whereby step c) is preferably conducted by freeze drying or by heating the bodies, thereby causing the liquid or part thereof to evaporate.

Step b) may also be conducted by submitting the mixture of a) to pressure, preferably under mixing and/ or increasing the temperature, and subsequently removing the pressure or part thereof, thereby causing the liquid to evaporate. For example, an extrusion process can be used. Hereby it is preferred that the mixture of the polymeric material, plasticiser, preferably including water, and optionaly the active ingredient, is introduced in an extruder, wherein the mixture is further mixed and heated, due to the mixing or due to applying heat, preferably such that the mixture therein forms a melt, and then dropping the pressure at the exit point where the extruded mixture (which can be formed into the desired form, for example granules) exits the extruder, whereby the liquid or part thereof evaporates, or preferably the water evaporates as steam from the extruded mixture. This results in formation of cells with spacings, as described above, 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 elastic article of the invention.

Step b) in the process may also be conducted by heating the mixture to cause the liquid or part thereof to evaporate, resulting in the formation of spacings, as above.

This can preferably done by feeding the mixture into a spray drying tower, preferably such that the mixture is fed through spray nozzles which form droplets of the mixture, and spray drying the droplets at conventional, resulting in granules of the elastic article.

19 The physical and/ or chemical introduction of gas or foaming. as mentioned above can be done by any known method, preferred are - physical foaming by gas injection (dry or aqueous route) optionally under mixing, high shear stirring (dry or aqueous route), gas dissolution and relaxation including critical gas diffusion (dry or aqueous route); - chemical, foaming by In-situ gas formation (via cherrucal reaction of one or more ingredients, including formation Of C02 by an effervescence system), steam blowing, LTV light radiation curing.

These foaming steps are preferably followed by a drying step or an additional drying step to remove excess liquid or part thereof, such as water. In particular, the drying step is at least done after the polymer matrix is formed, and optionally after the active ingredient is added, preferably as final step in the process. The drying step is done preferably such that the final elastic article 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. Also useful can be slow fluid bed drying or oven drying at modestly increased temperatures, such as 40-80'C, or even 40-60'C.

Preferred processes involve at least the step of formation of a mixture of polymeric material and a liquid, preferably a solution of polymeric material and a solvent, preferably comprising water, and adding a plasticiser (or as the case may be, additional plasticiser) to this. If the presence of the active ingredient in the matrix is required, this is also added to the mixture of polymeric material solvent and palsticiser. Alternatively, or in addition, it may be preferred that the matrix is formed around the active material, preferably a core of the active material and carrier material.

This is than further processed for example into bodies of the shape of the final article, for example particles or beads, and typically dried to obtain the articles. Preferably, a gas is added prior to the shaping step. Shaping steps Include granulation steps such Z as atomisation or spray-drying, extrusion, micro pastillisation, Freeze drying is a preferred process to dry the bodies to form the articles.

The following are preferred processes resulting in low dust or even nil dust particles, as measured with the stressed Heubach test described below, having a matrix with a Tg of below 1 O'C and an elastic modulus of below 0. SGNm as indicated in more detail in the following specific examples.

A first preferred process is as follows: The required amount of a solution of the polymer material (or a mixture of polymer and a liquid) is obtained, and for example (introduced) in a mix tank. Then the required amount of (a solution of) the active material, for example an enzyme solution is added and the required amount of plasticiser is added, and optionally other additional ingredients, such as stabilisers, fillers, densification agents etc. This is agitated to become a homogeneous Mixture. Preferably, a gas such as air can be introduced into the solution, by any of the methods above, preferably physically, by high sheer mIxing.

Then, particles are formed from this mixture by atomisation, preferably using a Positive Displacement pump to transfer the mixture solution to a spray nozzle (s), preferably using either single or multi-fluid nozzles to create liquid droplets. The liquid droplets are then frozen, preferably by passing through a refrigeration media (can include liquid nitrogen, freon, reffigeration oils)- Then, the frozen particles are transferred to a vacuum chamber, preferably having a temperature (as measured on the surface of the particles) below O'C. The frozen particles are preferably collected from the spray column and transferred without raising the temperature. The temperature of the walls and contact trays of the freeze dryer are preferably maintained below OC to keep the particles frozen.

A vacuum is applied, and the ftozen ice crystals will sublimate a gas form, resulting in cells in the particle. The total drying degree can be controlled with the level of 21 vacuum, and contact temperature of the chamber walls and trays. After the particles have been dried to the desired moisture c ontent, they will be free flowing. Then preferably., the particles can be classified via a variety of screens and or process equipment. 5 The optional step above, of introducing gas (bubbles) into the polymeric solution mixture has been found to give a much better impact resistance to the particle, reflected by its electric modules. The introduction of gas bubbles can be accomplished in a variety of ways,

In the atomisation step, the atomizing nozzle should preferably be located in a spray column with sufficient height to accomplish droplet freezing while gravity falling. The nozzle type can be of various designs - single fluid pressure nozzle, spinning insert, sonic, or multi-fluid nozzle. The important aspect is to disrupt the liquid stream to form discrete liquid droplets. As these droplets fall with gravity, they need to be cooled to freezing. The freezing media is preferably non- aqueous gas or liquid which can provide rapid freezing of the liquid droplets. The actual temperatures for cooling these droplets to form particles, is preferably below O'C and preferably below -20'C.

It may also be preferred that the above process is modified as follows: a gas, preferably C02 gas, is introduced in the mixture and the mixture is introduced in a spray drying tower, as above, thereby forming spray-dried foamed particles, which can be classffied if necessary. Preferably the inlet temperature in the tower is about 130T and the outlet temperature about 75'C and the spray rate is 12.5g/min.

For example a Niro Mobil Nfinor with two fluid nozzles can be used hereby. The resulting particle may be already of the required form, or may be submitted to further freeze drying under vacuum.

22 Another preferred process is as follows. The required amount of a solution of the polymer material is obtained (or alternatively, a powdered polymer can be used provided a liquid is added) and for example introduced in a mix tank. Then the required amount of plasticiser is added, and optionally other additional ingredients, such as stabilisers, fillers, densification agents etc. This is agitated to become a homogeneous mixture. Preferably, a gas such as air can be introduced into the solut. lon, by any of the methods above, preferably physically, by high sheer mixing.

Also, particles comprising the active ingredient and optionally other ingredients, such as fillers or carriers are prepared, for example by fluid bed coating, by charging first C cores' (typically when the actives care enzymes, these core particles are sugar or starch particles), to a fluid bed and spraying the active material or a solution of the active material onto these cores and then drying any solvent such as water from the 15 active solution off with warm fluidizing air.

Then, the polymeric mixture above is introduced onto these active/cores, for example via a positive displacement pump leading to an atomizing nozzle inside the fluid bed as described above. More than one nozzle can be used and it may be preferred that 20 different ingredients are added to the core via different nozzles.

23 The fluidizing air needs is preferably below O'C, preferably around -200C. Then, the fluidizing air freezes the polymeric mixture/solution onto the outside of the activecore. This is a critical parameter to control and typically the air temperature must be below O'C in order to quickly freeze the polymeric mixture/solution onto the core 5 particles.

Then preferably, the frozen particles thus obtained are transferred to a vacuum chamber, as above, and also classification may take place.

This technology results in particle of the invention comprising a matrix around the active ingredient. The optional step above, of introducing gas (bubbles) into the polymeric solution mixture has been found to give a much better impact resistance to the particle, reflected by its Young's Modulus.

Another preferred process is as follows: The required amount of a solution of the polymer material (or solid polymer and a suitable amount of liquid) is obtained, and for example introduced in a MIX tank. Then the required amount of (a solution of) the active material, for example an enzyme solution is added (into the mix tank) and the required amount of plasticiser is added, and optionally other additional ingredients, such as stabilisers, fffiers, densification agents. This is agitated to become a homogeneous mixture. Preferably, a gas such as air can be introduced into the solution, by any of the methods above, preferably physically, by high sheer mixing.

Then, the polymeric solution is pumped from the mix tank into an extruder or into a cavity with a die plate at the end. Before entering the extruder or cavity, gas can be injected into the mixture and for example be dispersed via a mechanical shear mixer or a static mixer.

As the extrudate exits the die plate, the change in pressure creates a slight puffing or swelling in the extrudate. The extrudate is then cut to the correct length with either a 24 die face cutter or with some other device (eg. heated wire, rotating plug cutter, etc The extrudates can optionally go through additional rounding steps to become more spherical. Process equipment that can accomplish this ffinction include (rotating pans, agglomeration pans, marumirizers, tumbling drums, mixing drums, etc.).

For example, a paste is prepared by mixing 75g PVOH, 15g Citric acid, 2g PEO and 22.5g glycerol in a Braun nuxer, high sheer, namely set at full speed for 40seconds: then 80g H20 and 80g enzyme was added and mixed at high sheer, namely set at full speed until a smooth foam had formed, approximately within 2mins. The foam was extruded from a I Oml syringe onto a plastic sheet. This was left for 24 hours to dry. Once dry the foam strips were cut into approximately I - 2mm. sections to form particles of the formula (dry) 63.2 polyvinyl alcohol, 191/o glycerol, 12.71% citric aicd, L 6% PEO, 4% water, 3.2% enzyme.

-2 The resulting particles had an elastic modulus of 0. 000 1 6GN. in The resulting particles give 0% dusting when tested in a stressed Heubach test, which indicated a very good impact robustness. (The stressed Heubach test is performed as known in the art, using equipment as supplied by Heubach Engineering GMbH, Germany, with the stressed modification of the rotation speed of the impeller being 75 + I rpm and the baffs being of Tungsten carbide and 82 grains each.).

Preferred moulding / pastillisation process:

A highly preferred process involves shaping particles of mixtures as described above by use of a mould; whereby mixtures as described herein are introduced in a mould and subsequently dried (freeze dried). Also preferred is such a process which uses pastille making equipment, whereby mixtures as described above, preferably comprising also introduced gas, are forced through a rotating perforated drum onto a moving conveyor belt, shaping into pastilles (droplets or particles). When dry or hardened, the thus formed particles or beads are removed from the conveyor belt by a scraper.

Preferably, the first step is to make a mixture of polymeric material and plasticiser, a liquid component, and optionally the active ingredient. Preferably, gas is introduced into this mixture as described herein. This must preferably be free from large undissolved particles which may block up the perforations in the drum. The mixture is preferably in the temperature range 0-50T. The mixture is pumped into a manifold that enters the rotating perforated drum and is parallel to the longitudinal axis of the drum. The mixture is pumped into the inner of the drum and, as the drum rotates, is brought into contact with an internal scraper bladed lying In contact and along the length of the inner surface of the perforated drum, paraHel to the feed manifold. The distance of the outside surface of the perforated drum is within the height of the desired particle height (which is less than the diameter of the perforations) but not touching a moving conveyor belt or a rotating smooth surfaced drum at the point where the internal scraper is in contact with the inner surface of the perforated drum, the tangential speed of the perforated drum matched by the speed of the conveyor belt or the tangential speed of the smooth surfaced drum. As the mixture is forced through the perforations, which are typically in the size range 300 - 2000Lrn (but may be smaller or larger), it is deposited onto the surface below. The rotation of the perforated drum shears the feed material away from the material on the smooth surface thus leaving a droplet, or pastflle, which will form the required particle. These pastilles can be set by either chilling or by evaporation of some or aff of the solvent fluid. If chilling is required the temperature of the conveyor belt or smooth surfaced drum may be in the range ambient to -20'C. If evaporation of a solvent is required, then this can be achieved by heat conduction from the conveyor belt which may be in the range ambient to 70T, by drying air (which may be heated up to MOT to reduce drying time) passing over the surface of the pastilles, or both. Then, they resulting particles are removed from the drum or conveyor belt by a scraper. This removal process may be improved by the use of a suitable lubricant (release agent) on the drum, such as silicone oil. This lubricant or release agent may show an added benefit to the particle by reducing adhesive properties between the 26 polymeric mixture and the belt/drurn and thus increasing the pastille height, if this is a desirable feature.

An example of this process is as follows:

4700g of a 33%w/w solution of polyvinyl alcohol (weigth average M.W being from 30,000 to 70,000) is mixed with 159.3g of glycerol and 109.8g of citric acid in a high shear mixer until a smooth foam is formed. This mixture is transferred into a feed tank, and using a gear pump, it is pumped into micropastillisation equipment, for example as supplied by Sandvik Process Systems, Totowa New York, using a perforated drum with perforations of I mm diameter, spaced 2.5mm apart. The apparatus deposits pastilles onto a smooth surfaced drum coated with a film of silicone oil and heated to -30T. When one quarter of the drum is covered by pastilles, the drum is stopped from rotating. The pastilles are dried using a hot air heater until the surfaces of the pastilles are dry to the touch. The resulting particles are then scraped off and collected.

The resulting particles had a elastic modulus of 0.00 1 GN. M-2.

The resulting particles give 0% dusting when tested in a stressed Heubach test, which indicated a very good impact robustness. (The stressed Heubach test is performed as known in the art, using equipment as supplied by Heubach Engineering GMbK Germany, With the stressed modification of the rotation speed of the impeller- being 75 + I rpm and the balls being of Tungsten carbide, 82 grams each.) Another example of making foamed articles of the invention, in the form of tablets, beads or particles, is as follows:

Apparatu: Microbalance, graduated I 00ml flask, Kenwood "Chef' food processor with provided whisk and mixing bowl, glass or plastic moulds, spatula.

27 Chemicals poly (vinyl alcohol) (Aldrich chemicals, molecular weight MIA= 30-70k), Glycerol (99 %, Aldrich chemicals), Citric Acid (Aldrich, Citric Acid, USP Anhydrous), distilled water, dry ice (or solid phase COA thermally insulated box.

Procedure 1. Weigh 50 0.2 grams of PVA, 30 0.2 grams of glycerol, 20 0.2 grams of citric acid.

2. MIX the PVA, glycerol and Citric acid using the mixer set a low speed (mark 2.

low sheer).

3. Add 50 I ml of water gradually to the dry mix maintaining the mechanical mix for 2 minutes. A smooth gel should be obtained.

4. Increase the mix speed high sheer to the maximum setting (mark 8). Add 10-20 ml of water until a PVA foam is forming. Maintain high shear mixing for 3 minutes.

5. The active ingredients, for example from 2- 10 gram of enzyme, are progressively added to the foam under a maintained mechanical mixing so that a uniform active foam is obtained.

6. Stop mixirtg. Spread the PVA foam in moulds avoidi.ng any collapsing of the structure.

7. Place the filled moulds in a thermally insulated box 1/3 filled with dry ice. Leave to freeze for 5 hours.

8. Quickly place frozen samples in a vacuum freeze-dryer (Edward XX) for 24 hours.

9. Remove dried sample from moulds.

Any active ingredient can be added in step 5, at any level, normally up to about 50 grams, for example fabric softeners, bleaching species, nonionic surfactants.

This was also repeated by using for example 40wt% polycarboxylic acid polymer, 30wt% diethyleneglycol, 15wt% amine oxide and as active ingredient 15wt% enzyme, softening clay etc.; and repeated by using 40wt% polycarboxylic acid polymer, 30wt% polyethylene glycol, 15wt% amine oxide and acid LAS (I 1) and as active ingredient 15wt% enzyme, softening clay etc.

28 Another example of making foamed articles of the invention, in the form of tablets, beads or particles, is as fbllows Apparatus: as described in the above example Chemlcals Poly (vinyl alcohol) (Aldrich chemicals, molecular weight Mw-- 30-70k), Glycerol (99 %, Aldrich chemicals), Citric Acid (Aldrich, Citric Acid, USP Anhydrous), Sodium carbonate (Aldrich, Anhydrous), Dodecyl Sulphate surfactant (Aldrich), distilled water, Petn dish (diameter 90 mm), Oven (set at 45 T 2Q Process:

1 - Weigh 50 --0.2 grams of PVA, 30 0.2 grams of glycerol, 20 0.2 grams of citric acid, 20 0.2 grams of sodium carbonate, and 2 0.2 grams of dodecyl sulphate, 2. Nfix the PVA, glycerol, citric acid and dodecyl sulphate using the mixer set a low speed (mark 2). I Add 50 I ml of water gradually to the dry mix maintaining the mechanical rrux for 2 minutes. A smooth gel should be obtained. 4. Add the active ingredient, for example 5 gram enzyme, and sodium carbonate and mix Vigorously for 30 second until a fully expanded foam is obtained 5. Spread the foam in petri dish in a uniform I cm thick layer 6. Place petri dish in 40 T oven for 24 hours.

7. Remove the dried foam film from mould.

Any active ingredient can be added in step 4, at any level, normally up to about 50 grams, for example fabric softeners, bleaching species, nonionic surfactants.

This was repeated by using 55wt% polycarboxylic acid polymer, 20wt% anhydrous sodium carbonate and 25wt% enzyme, softening clay etc., and repeated by using 45wt% polycarboxylic acid polymer, 15wt% polyethylene glycol, 20wt% anhydrous sodium carbonate and 20wt% enzyme, softening clay etc.

29 Other preferred modifications In the above processes, other polymer material mixtures of for example PVA and PVP or PEG were also used, and other plasticisers were used. Also, instead of the enzymes, other actives such as bleach or bleach activators or perfumes were used.

Preferred modification was also in any of the above processes that the gas introduced is carbon dioxide,C02. This was done my introducing actual C02gas into the polymer material/ plasticiser but this could equally be done by ingredients (such as effervescence sources) which chemically formC02in the mixture. 10 Form of elastic article The elastic article can be made into any form, by any conventional shaping method, some methods being described in detail above. Preferred may be that the elastic article is in the form of a particles, including pastilles and beads or in the form of tablets. 15 The particles can be made by any granulation method. for example by granulation techniques such as atomisation, use of moulds or pastillisation equipment, grinding larger shapes of the elastic article, spray-drying, extrusion, as also described above. Preferred elastic particles herein have a mean particle size of from 10 to 5000 20 microns, more preferably from 50 to 4000 microns or even to 2000 microns, even more preferably from 100 to 1500 microns or even form 200 or even 300 microns to 1000 microns. The article herein may have a layered structure, having for example, a core of the 25 active ingredient, enclosed by a layer of matrix, optionally coated or for example, a core of (part of) the matrix, enclosedwith a layer ofthe a,:,,!%-e and +hen coated. -,"or L example with more of the matrix. The elastic article may also be in the form of a sheet, which can be obtained by any method, preferably by forming the sheet in a mould, as described above. When the elastic article is in the form of a sheet, the sheet 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. 0 1 to 400 microns, more preferably from 0.05 to 200 microns, or even more preferably from 0. 1 to 100 nucrons, or even 0. 1 to 50 microns.

Additional In-gredient The elastic article of the invention may preferably contain additional ingredients, such as process aids, stabilisers, lubricant, dispensing aids, pH regulators, solubilisers, including hydrotropes and disintegrating aids, densification aids, dyes, whitening agents, fillers, antioxidants and scavengers, perfumes.

Preferred additional agents are in particular effervescence sources, in particular based on organic carboxylic acids and carbonate sources.Preferred may be the use of citric acid, malic acid, maleic acid, fumaric acid or mixtures thereof, and for example salts (sodium) of percarbonate, carbonate. and/ or bicarbonate. These may for example be comprised in the matrix. Preferred may be that the acid is present in the matrix and the carbonate in a different layer or core, or vise versa. It has been found that in particular the presence of an acidic material improves the dissolution and/or dispersion of the elastic article 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 elastic article with cationic species present in the aqueous medium.

Phosphonate-based such as Chelating agents may also be preferred additional ingredients.

Preferred may also be to incorporate (in the polymer material) disintegrating polymers or water-swelleable polymers, which aid dissolution of the article. Thus, these may form part of the pol,,,-nieric matrix herein. Examples of such aids are described in EP851025-A and EP466484-A Perfumes are also preferred ingredients of the article herein. Surfactants may also be added to the article, including certain nonionic surfactants which may also give a lubrication affect.

31 It may be preferred that inorganic salts or silicates are present. Including zeolites and/ or phosphates.

Preferred additional ingredients are also ammonium compounds such as ammonium sulfate., ammonium citrate, and also granular urea, guaruidine hydrochloride, gaunidine carbonate, guanidine sulfonate, granular thiourea dioxide, Colouring agent such as iron oxides and 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 I% by weight of the article.

Highly preferred additional ingredients include urea. and/ or inorganic salts. Highly preferred may also be cross-linking agents, changing the crosslinking degree of the polymer material in the matrix. Borate may be useful.

Highly preferred may be that the article is coated with a coating agent, as known in the art, by any coating process. Preferred may be coating agents containing organic acids or salts, inorganic salts, additional polymers, having Tg of higher than 601C, typically higher than 70T.

Highly preferred is that the elastic article comprises (as pH-controller or dissolution aid) an acid such as citric acid, acetic acid, acetic acid glaciaL finnaric acid, hydrochloric acid, malic. acid, maleic acid, tartaric acid, nitric acid, phosphoric acid, sulfuric acid, pelargonic acid, launc acid. Buffering agent which also boric acid, sodium acetate, sodium citrate, acetic acid. potassium phospates and the likes.

Compositions comprising the elastic article The elastic article may be incorporated in any compositions which requires active ingredients to be protected against moisture during storage, against chemical reactions 32 with other ingredients, rillgration or phase separation of ingredients, or protection against physical forces.

In particular, the elastic article is useful in cleaning compositions, fabric care compositions, personal care compositions, cosmetic compositions, pharmaceutical compositions. These compositions may are typically solid. 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, is 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 article 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.

In personal-care products it may be highly preferred to include cationic organic compounds, such as cationic surfactants. It can be preferred that the compositions comprise one or more other ingredient which can reduce dermatitis or compounds which can help the healing of the skin, metalcontaining compounds, in particular zinc-containing compounds, Vitamins and cortisone's, and also compounds to soften the skin such as vaseline, glycerin, tnethyleneglycol, lanolin, paraffin and another group of polymers extensively employed by pharmaceutical and cosmetic manufactures, as also described herein.

33 The pharmaceutical compositions, cosmetic compositions and personal care compositions can be of any form and purpose. Preferred are pharmaceutical powders and tablets. The elastic article can also be incorporated in absorbing articles, for example to release the actives of the elastic article 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.

34

Claims

1. An elastic article comprising a) an active ingredient; b) a matrix formed from a polymeric material and a plasticiser, provided that when the plasticiser consists of water, the level is at least 3% by weight, whereby the article is capable of delivering the active to a liquid environment, and whereby the matrix has a glass transition temperature (Tg) below STC, preferably below 4TC, and whereby the active ingredient or part thereof may be present in the matrix.

2. An article as in claim 1 whereby the active ingredient is active in aqueous environment and the article is water-dispersable, water-disintegrating or water is soluble, preferably the matrix is water-soluble.

3. An article according to claim 1 or 2 whereby the matrix has a Tg between -20'C and 2TC, preferably even between ATC and ITC, and an elastic modulus of less than 1 GN. M-2 preferably less than 0. 1 GN. M-2, or even less than 0. 0 1 GN. m-2.

4 An elastic article according to any of claims 1 to 3, which is in the form of a foam which is a stable upon contact with air and unstable upon contact with water, said elastic foam article preferably having an elastic modulus of less than 0. 1 GN. M-2or even below 0. 0 1 GN. m-2.

5. An elastic article according to any preceding claim comprising from 30% to 90% by weight of the matrix and from 5% to 70% by weight of water and from 1% to 15% by weight of a plasticiser, preferably including at least 3% by weight of free moisture.

6. An article according to any of claims 1 to 5 obtainable by a process comprising the step of a) obtaining a mixture of a polymeric material and a plasticiser, preferably W water and another plasticiser; b) chemically or physically introducing gas in said mixture of polymeric material and waterl c) prior to step b) and/or simultaneously with step b) and/ or subsequently to step b), addition of the active ingredient to the mixture of polymer material and water; d) shaping of articles of the resulting mixture of step c).

whereby preferably one or more of steps a) to d) are followed or accompanied by removal of part of the water, if present.

7. An article according to claim 6, whereby step c) of the process as in claim 6 comprises the step of obtaining a body comprising the active ingredient or part thereof and enclosing said body with the mixture of step b).

8. An article as in claim 6 or 7 whereby in step a) the mixture is an aqueous mixture and after or in step b), c) and/ or d) of claim 6 part of the water is removed such that the resulting article comprises at least 3% by weight of free-moisture.

9. An elastic article according to claim 4, whereby the foam article comprises cells. obtainable by a process comprising the steps of a) formation of a mixture of the polymeric material, the active material, plasticiser and a liquid, whereby the liquid and the plasticiser may be the same compound; b) shaping of bodies from the mixture of claim b) and 36 b) evaporation of the liquid or part thereof to form spacings in the mixture which form the inner area of the cells of the article, whereby step c) is preferably conducted by freeze drying or by heating the bodies, thereby causing the liquid or part thereof to evaporate.

10. An elastic article according to any preceding claim whereby the polymeric material comprises a water-soluble polymer, preferably a polyvinylalcohol.

11. An elastic article according to any preceding claim which has a relative density of 0. 05 to 0. 9, preferably 0. 3 to 0. 7,

12. An elastic article according to any preceding claim comprising closed and open cells, preferably the ratio of closed to open cells being at least 1: 1.

13. An elastic article according to any preceding claim whereby the active ingredient is a cleaning product ingredient, fabric care ingredient, pharmaceutical ingredient or cosmetic ingredient, preferably selected from enzymes, perfumes, surfactants, brighteners, dyes, suds suppressers, bleaches, bleach activators, fabric softeners, fabric conditioners, antibacterial agents, effervescing systems and rnixtures thereof

14. An elastic article according to claim 13 whereby the active ingredient comprising at least an enzyme.

15. An elastic article according to any preceding claim which is in the form of a (7ranule, bead or tablet.

16 A according to claim 15 in the form of a particle or bead having a mean particle size of from 50 to 4000 microns, preferably from 100 to 1500 microns.

37

17. An elastic article according to any preceding claim- comprising a cleaning composition, fabric care composition cosmetic composition or pharmaceutical composition.

18. A cleaning composition, fabric care composition, cosmetic composition, personal care composition or pharmaceutical composition comprising the elastic article according to any of claims 1 to 16.

19. A process as in claim 6, 7 or 9.

20. A process as in claim 19 comprising the step of introducing gas in a mixture comprising at least the polymeric material, water, another plasticiser and optionally the active ingredient to form a foam and subsequently forming particles, beads or tablets form the foam, by use of a spraying process, extrusion process, moulding process or micropastiflisation process, the process comprising at least one drying step.

21. Use of an elastic article according to any of claims 2 to 17 to deliver active ingredients to an aqueous environment, preferably. the active ingredients being detergent active ingredients and the aqueous environment being the wash water.

22. Use of a elastic article according to any of claims 2 to 17 in cleaffing compositions, fabric care compositions, personal care compositions, cosmetic compositions or pharmaceutical compositions, preferably to incorporate therein active ingredients selected from enzymes, perfumes, surfactants, brighteners, dyes, suds suppressers, bleaches, bleach activators, fabric softeners, fabric conditioners, antibacterial agents, effervescing systems, and nfixtures thereof