The present invention is in the field of biodegradable builders. In particular it relates to a particle comprising an aminocarboxylic builder, especially methylglycine diacetic acid (MGDA) or salts thereof. The particle has a core-shell structure, the aminocarbocylic builder is mostly present in the core and the shell is mainly formed by an inorganic salt. The particle presents high flowability and is stable to high ambient humidity during transport, storage, handling and even when it is present in a detergent composition, even if the detergent is phosphate free. In addition, the shell helps prevent undesirable interactions with other detergent components.
Traditionally phosphate builders have been used in detergent formulations. Environmental considerations make desirable the replacement of phosphate by more environmentally friendly builders. Apart from cleaning repercussions, the replacement of phosphate can impair the stability of the detergent. Phosphate is a good moisture sink contributing to moisture management and stability of the detergent. The majority of the builders which can be used as replacement for phosphate are incapable of acting as moisture sinks—furthermore they are usually hygroscopic, contributing to the instability and degradation of the detergent. This has a greater impact in detergents which comprise moisture sensitive ingredients such as bleach and enzymes.
A consequent problem found with many phosphate replacements, such as aminocarboxylic builders and in particular MGDA and salts thereof, is their instability and difficulty in handling under the high ambient temperature and humidity conditions that can be found in manufacturing plants or during transport and storage. This problem can be particularly acute during hot and humid summer months or during a rainy season. Particulate materials can lose their flowability and—in cases in which the materials are highly hygroscopic—they can become sticky, crusty or turn into liquids, making them unsuitable for use in detergent formulations.
Aminocarboxylic compounds such as methylglycine diacetic acid and salts thereof are suitable compounds as phosphate replacement in detergent compositions. The use thereof is, however, in most cases restricted to their use in liquid applications. This is due to the fact that these materials in solid form tend to be highly hygroscopic. Hence in typical manufacturing conditions, storage and/or transport, they can lose their stability and even return to its liquid form. It is possible to avoid many of these issues by the use of protective engineering measures such as dehumidification of the ambient air. However these can be very expensive to implement throughout the entire manufacturing process—especially in large manufacturing plants.
There have been several attempts to convert methylglycine diacetic acid and salts thereof into solid particles. Some of the processes are quite cumbersome and sometimes the resulting particles are not totally satisfactory from a handling, transport, storage and in-product stability viewpoint. Other drawbacks found with some of the particles disclosed in the literature is that the particles include additional materials that can be inert in terms of cleaning, thereby contributing to the cost of the product without providing any benefits and in some cases even having negative impact on cleaning, such as leaving residues on the cleaned items. A further drawback is the yellowing of some particles that negatively impact in the aesthetic of products.
Turning to the existing art, U.S. 2008/0045430 discloses a mixed powder or mixed granule containing at least 80% by weight of a mixture of (a) from 5 to 95% by weight of at least one glycine-N,N-diacetic acid derivative of general formula MOOC—CHR—N(CH2COOM)2 where R is C1-12 alkyl and M is alkali metal, (b) from 5 to 95% by weight of at least one polyethylene glycol or of at least one nonionic surfactant or of a mixture thereof or of a polymer selected from the group consisting of polyvinyl alcohols, polyvinylpyrrolidones (PVP), polyalkylene glycols and derivatives thereof. The particles of '430 comprise materials that may not contribute to cleaning and can leave residues on the cleaned items. Moreover, the dissolution of the particles seems to rely on the melting or dissolution of component b). The current tendency on automatic cleaning processes, such as laundry and dishwashing, is to use lower temperatures. There is a risk that the particles would not dissolve sufficiently rapid at low temperature. Although, the particles have improved handleability there is still room to improve their physical properties especially in conditions of high ambient humidity.
In WO 2009/103822 is stated that particles of MGDA made via conventional spray drying processes tend to be fine and dusty, have a high tendency to absorb water at ambient conditions and lose their free-flowiness. The resulting products are hygroscopic, resulting in sticky powder and even in lumps. Different routes have been developed for preparing solids from solutions of glycine-N,N-diacetic acid derivatives to try to overcome these drawbacks.
In EP 845456, the crystallisation of a very concentrated composition of the glycine-N,N-diacetic acid derivatives, containing between 10 and 30% moisture is described. By this process large particles with low hygroscopicity and good flowability can be obtained. Crystalline materials are, in most cases, less hygroscopic than the amorphous for due to the greater difficulty of moisture penetration into the crystal structures. However, this process requires dedicated equipment, and the low moisture composition has been found to be very difficult to process. Consequently, such a process is quite expensive.
WO2009/092699 proposes a process for the preparation of free flowing MGDA granules having low hygroscopicity, probably based on crystallisation of the MGDA. This comprises heating a concentrated slurry comprising MGDA and spray granulating said slurry. The process requires the preparation of the concentrated slurry before processing further and this could be difficult depending on the solids concentration used. The process is also limited by the requirement that the drying air used in the spray-granulation has to be less than 120° C. This means that drying rates will be limited compared to processes using higher drying air temperatures. The particles prepared according to '699 are crystalline. It is broadly accepted that MGDA in crystalline form is less hygroscopic and presents more favourable features for its use in detergents, however a longer residence time and a more controlled conditions are required in order to produce a crystalline material and this will have cost implications.
WO20100133617 discloses a method for producing a spray powder containing glycine-N,N-diacetic acid derivative, starting from an aqueous solution containing the one or more glycine-N,N-diacetic acid derivatives, which is spray-dried by adding air, characterized in that—the aqueous solution contains the one or more glycine-N,N-diacetic acid derivatives at a fraction of >84 wt. % relative to the total weight of the dry mass, and that—the spray drying occurs in a drying apparatus, to which the aqueous solution and the air are fed in parallel flow, with a temperature gradient between the aqueous solution and the air in the range of 70 to 350° C., and that—in the drying apparatus, the aqueous solution is atomized into fine liquid droplets by being guided onto one or more disks, which rotate at a circumferential speed of 100 m/s, or by being compressed by means of a pump to a pressure of 20 bar absolute and introduced into the drying apparatus at this pressure by means of one or more nozzles. The MGDA in this form is not suitable for consumer use and needs to be processed further. The equipment needed for spraying the MGDA liquid is more complicated than other alternatives, for example high pressure pumps are needed.
The objective of the present invention is to provide a particle which maintains its physical structure and is stable during storage, transport, manufacture and at the same time it is stable and maintains its appearance in detergent compositions even in phosphate free detergents.
According to a first aspect of the invention, there is provided a particle. The particle has a core-shell structure. The particle comprises an aminocarboxylic builder and a water-soluble inorganic salt. Essentially the builder is found in the core and the salt is essentially coating the builder. The salt forms a barrier layer that surrounds the builder, this shell-core structure provides good protection for the builder.
The term “particle” as used herein includes a single particle and a plurality of particles. For the purpose of the present invention the term “aminocarboxylic builder” includes aminocarboxylic acids, salts and derivatives thereof. Preferably the aminocarboxylic builder is an aminopolycarboxylic builder, more preferably a glycine-N,N-diacetic acid or derivative of general formula MOOC—CHR—N(CH2COOM)2 where R is C1-12 alkyl and M is alkali metal. Especially preferred aminocarboxylic builder for use herein is methylglycine diacetic acid (MGDA), more preferably alkali metal salts, even more preferably sodium, potassium and mixed sodium/potassium salts. Especially preferred for use herein is the tri-sodium salt, more preferably the tri-sodium salt of MGDA.
The inorganic salt of the particle of the invention is water-soluble. By “water-soluble” herein is meant a salt which has a solubility in distilled water of more than 1%, preferably more than 5%, even more preferably more than 10% and especially more than 15% by weight of the solution at 20° C.
In preferred embodiments the aminocarboxylic builder is present in the particle in amorphous form, preferably the aminocarboxylic builder is selected from methylglycine diacetic acid and salts thereof. A material is considered “amorphous” if at least 40%, more preferably at least 60%, even more preferably at least 80% and especially at least 90% of the material, by weight thereof is amorphous, as determined by calculating the relative % crystallinity from X-ray diffraction spectra in the 10-40 degree range of 2 theta, using the Ruland method, as described in detail in the publication: Ruland, W. (1961). Acta Cryst. 14, 1180-1185, entitled: X-ray Determination of Crystallinity and diffuse Disorder Scattering. In amorphous material the atoms are arranged in a random way. In crystalline material the atoms are arranged in a regular pattern. Amorphous material lacks a coherent, long-range structure. When subjected to X-ray diffraction at room temperature, amorphous material will present a very broad diffraction peak often known as a halo, whereas crystalline material will present one or more sharp narrow diffraction peaks.
Amorphous organic materials are generally more hygroscopic and have less favourable properties, in terms of stability, than crystalline materials. Amorphous materials however are usually cheaper to produce than crystalline materials. Once the material is produced in amorphous form care needs to be taken to ensure its compatibility and stability in detergent compositions. The particle of the invention has been found to be stable and robust during the detergent manufacture process and when part of a detergent composition. The core-shell structure seems to be critical in order to provide the stability and robustness of the particle.
The water-soluble salt is preferably selected from the group consisting of sulphate, citrate, carbonate, bicarbonate, silicate and mixtures thereof. Especially preferred for use herein is sodium sulphate. Particles wherein the shell is mostly sodium sulphate present a really good stability profile and also present a good solubility profile. Furthermore, sodium sulphate provides a particle with good compatibility with detergent ingredients. Burkeite is another water-soluble salt preferred for use herein.
The particle can be highly active, this makes it space efficient for its use in detergents. In preferred embodiments the core represents from about 50, preferably from about 60% and more preferably from 70% to about 98% by weight of the particle. In some case it is useful for the core to comprise detergent active ingredients. Especially useful has been found the presence of carbonate in the particle of the invention. The presence of carbonate makes the particle highly suitable for use in automatic dishwashing detergents. In another preferred embodiment the shell represents from about 2%, preferably from about 5% and more preferably from about 10% to about 50% by weight of the particle.
In preferred embodiments, the particle of the invention has a pH in 1% wt distilled water at 20° C. of at least 7, more preferably at least 9, even more preferably at least 10. Particles with this pH are more suitable for use in detergent compositions, especially in automatic dishwashing detergent compositions, that usually are alkaline.
In a preferred embodiment the particle of the invention has a bulk density of at least 650 g/l, this makes the particle space efficient and help to avoid segregation in detergent compositions.
Preferably the particle of the invention has a weight geometric mean particle size of from about 400 μm to about 1200 μm, more preferably from about 500 μm to about 1000 μm and especially from about 700 μm to about 900 μm. Preferably the particle has a low level of fines and coarse particles, in particular less than 10% by weight of the particle are above about 1400, more preferably about 1200 and/or below about 400, more preferably about 200 μm. These mean particle size and particle size distribution further contribute to the stability of the particle. In especially preferred embodiments, from the stability point of view, the particle has a weight geometric mean particle size of from about 700 to about 1000 μm with less than about 3% by weight of the particle above about 1180 μm and less than about 5% by weight of the bleach below about 200 μm. The weight geometric mean particle size can be measured using a Malvern particle size analyser based on laser diffraction.
According to a second aspect of the invention, there is provided a process for making the shell-core particle of the invention. The process comprises the steps of:
In a preferred embodiment the intermediate particle is compacted, ground and sized and more preferably dried after it has been ground and sized.
Preferably the intermediate particle resulting from step c) has a level of moisture of from about 0.1 to about 30%, more preferably from about 0.2 to about 10%, from about 0.5 to about 5% by weight of the particle, this level of moisture contributes to the ability of the particle to be coated by an aqueous solution of the inorganic salt.
According to the last aspect of the invention, there is provided a detergent composition, preferably an automatic dishwashing detergent composition, more preferably a phosphate free automatic dishwashing detergent composition. The particle of the invention presents good stability during the manufacture of the detergent and in the detergent. The detergent provides good cleaning.
The present invention envisages a particle, having a core-shell structure, wherein the core contains an aminocarboxylic builder and the shell contains an inorganic salt, preferably water-soluble. The particle has good stability during storage, transport, manufacture and even in stressed detergent matrixes such as phosphate free detergents. There is also provided a process for making the particle. The process not only produces a very robust particle in term of physical and chemical stability but the particle is also very robust in terms of processability. Finally, there is also provided detergent composition preferably an automatic dishwashing detergent composition, more preferably phosphate free comprising the core-shell particle of the invention.
Preferably the aminocarboxylic builder that forms the core of the particle of the invention is an aminopolycarboxylic builder, more preferably a glycine-N,N-diacetic acid or derivative of general formula MOOC—CHR—N(CH2COOM)2 where R is C1-12 alkyl and M is alkali metal. Especially preferred aminocarboxylic builder for use herein is methylglycine diacetic acid, more preferably alkali metal salts thereof, even more preferably sodium, potassium and mixed sodium/potassium salts. Especially preferred for use herein is the tri-sodium salt.
Preferred aminocarboxylic builders include MGDA (methyl-glycine-diacetic acid), GLDA (glutamic-N,N-diacetic acid), iminodisuccinic acid (IDS), carboxymethyl inulin and salts and derivatives thereof. MGDA (salts and derivatives thereof) is especially preferred according to the invention, with the tri-sodium salt thereof being preferred and a sodium/potassium salt being specially preferred for the favourable hygroscopicity and fast dissolution properties of the resulting particle.
Other suitable aminocarboxylic builders include; for example, aspartic acid-N-monoacetic acid (ASMA), aspartic acid-N,N-diacetic acid (ASDA), aspartic acid-N-monopropionic acid (ASMP), iminodisuccinic acid (IDA), N-(2-sulfomethyl) aspartic acid (SMAS), N-(2-sulfoethyl) aspartic acid (SEAS), N-(2-sulfomethyl) glutamic acid (SMGL), N-(2-sulfoethyl) glutamic acid (SEGL), IDS (iminodiacetic acid) and salts and derivatives thereof such as N-methyliminodiacetic acid (MIDA), alpha-alanine-N,N-diacetic acid (alpha-ALDA), serine-N,N-diacetic acid (SEDA), isoserine-N,N-diacetic acid (ISDA), phenylalanine-N,N-diacetic acid (PHDA), anthranilic acid-N,N-diacetic acid (ANDA), sulfanilic acid-N,N-diacetic acid (SLDA), taurine-N,N-diacetic acid (TUDA) and sulfomethyl-N,N-diacetic acid (SMDA) and alkali metal salts and derivative thereof.
Preferably, the particle of the invention is made by a process that involves the step of drying a solution, preferably an aqueous solution, containing the aminocarboxylic builder, followed by coating the resulting particle with the inorganic salt.
Preferred inorganic salt for use herein is sulphate, in particular sodium sulphate. It has been found useful to use a saturated sulphate solution at 25° C. (i.e. a solution comprising approximately 25% by weight of the solution of sodium sulphate). This is optimum from a particle formation viewpoint because it simplifies manufacture of the particle.
An acidifying agent can be added to the aminocarboxylic builder solution to achieve a desired pH, including organic acids and mineral acids. Organic acids can have one or two carboxyls and preferably up to 15 carbons, especially up to 10 carbons, such as formic, acetic, propionic, capric, oxalic, succinic, adipic, maleic, fumaric, sebacic, malic, lactic, glycolic, tartaric and glyoxylic acids. Mineral acids include hydrochloric and sulphuric acid. Sulphuric acid is especially preferred for use herein because it forms sodium sulphate on neutralisation. Also sulphuric acid can be added as the concentrated form and hence minimise the amount of additional water that would need to be dried off.
The particle of the invention is obtainable, preferably obtained, by a process comprising the steps of:
The particle obtainable and preferably obtained according the above process presents very good stability properties and robustness during handling, manufacture, storage, transport and when it forms part of detergent compositions, even in stressed detergent matrixes such as those found in phosphate free products.
The first step (step a)) for the preparation of the particle of the invention requires to provide a solution comprising the aminocarboxylic builder, preferably MGDA. The aminocarboxylic builder can be in acid form or in the form of a salt or derivative thereof. If the aminocarboxylic builder is in salt form having a pH above 11 an acidifying agent, preferably sulphuric acid, is added to form a mixture with a pH of less than 11. Alternatively, sodium bicarbonate can be used. This is desirable as it forms carbonate, which in an active component in detergents.
The solution can then be transferred preferably through at least one pump to drying equipment. Any equipment capable of drying the mixture can be used, for example a fluidised bed, a spray-drying tower, etc. The preferred drying method for use herein is air atomization. If the mixture is going to be air atomized then the solution is pumped to a nozzle, from where the solution leaves in the form of a jet. This jet is broken by pressurized air, producing a spray. This spray is usually finer and can have a narrower size distribution than that obtained with a traditional spray drying process. More homogeneous particle size implies better moisture control, that it is critical in the case of hygroscopic materials.
Alternatively an aqueous solution of the builder can be pumped to the drying equipment in conjunction with sulphuric acid and sodium hydroxide and the resulting mixture would be air atomized to create the intermediate particle.
Once the intermediate particle is obtained, it can be processed further to modify its granulometry and density and then dried. More dense particles have been found to be more robust and stable. The intermediate particle can be subjected to any compacting operation. Preferred for use herein is roller compaction. The compacting step can be followed by a grinding step with recycle to achieve a specific granulometry.
The intermediate particle is then coated with the inorganic salt. Preferably the coating takes place in a fluidized bed, more preferably with a heated air stream such that the material is highly fluidized.
The detergent composition can comprises in addition to the particle of the invention one or more detergent active components which may be selected from surfactants, enzymes, bleach, bleach activator, bleach catalyst, polymers, dying aids and metal care agents.
Surfactants suitable for use herein include non-ionic surfactants. Traditionally, non-ionic surfactants have been used in automatic dishwashing for surface modification purposes in particular for sheeting to avoid filming and spotting and to improve shine. It has been found that non-ionic surfactants can also contribute to prevent redeposition of soils.
Preferably the composition of the invention comprises a non-ionic surfactant or a non-ionic surfactant system, more preferably the non-ionic surfactant or a non-ionic surfactant system has a phase inversion temperature, as measured at a concentration of 1% in distilled water, between 40 and 70° C., preferably between 45 and 65° C. By a “non-ionic surfactant system” is meant herein a mixture of two or more non-ionic surfactants. Preferred for use herein are non-ionic surfactant systems. They seem to have improved cleaning and finishing properties and better stability in product than single non-ionic surfactants.
Phase inversion temperature is the temperature below which a surfactant, or a mixture thereof, partitions preferentially into the water phase as oil-swollen micelles and above which it partitions preferentially into the oil phase as water swollen inverted micelles. Phase inversion temperature can be determined visually by identifying at which temperature cloudiness occurs.
The phase inversion temperature of a non-ionic surfactant or system can be determined as follows: a solution containing 1% of the corresponding surfactant or mixture by weight of the solution in distilled water is prepared. The solution is stirred gently before phase inversion temperature analysis to ensure that the process occurs in chemical equilibrium. The phase inversion temperature is taken in a thermostable bath by immersing the solutions in 75 mm sealed glass test tube. To ensure the absence of leakage, the test tube is weighed before and after phase inversion temperature measurement. The temperature is gradually increased at a rate of less than 1° C. per minute, until the temperature reaches a few degrees below the pre-estimated phase inversion temperature. Phase inversion temperature is determined visually at the first sign of turbidity.
Suitable nonionic surfactants include: i) ethoxylated non-ionic surfactants prepared by the reaction of a monohydroxy alkanol or alkyphenol with 6 to 20 carbon atoms with preferably at least 12 moles particularly preferred at least 16 moles, and still more preferred at least 20 moles of ethylene oxide per mole of alcohol or alkylphenol; ii) alcohol alkoxylated surfactants having a from 6 to 20 carbon atoms and at least one ethoxy and propoxy group. Preferred for use herein are mixtures of surfactants i) and ii).
Another suitable non-ionic surfactants are epoxy-capped poly(oxyalkylated) alcohols represented by the formula:
R1O{CH2CH(CH3)O}x{CH2CH2O}y{CH2CH(OH)R2} (I)
Preferably, the surfactant of formula I, at least about 10 carbon atoms in the terminal epoxide unit {CH2CH(OH)R2}. Suitable surfactants of formula I, according to the present invention, are Olin Corporation's POLY-TERGENT® SLF-18B nonionic surfactants, as described, for example, in WO 94/22800, published October 13, 1994 by Olin Corporation.
Amine oxides surfactants useful herein include linear and branched compounds having the formula:
These amine oxide surfactants in particular include C10-C18 alkyl dimethyl amine oxides and C8-C18 alkoxy ethyl dihydroxyethyl amine oxides. Examples of such materials include dimethyloctylamine oxide, diethyldecylamine oxide, bis-(2-hydroxyethyl)dodecylamine oxide, dimethyldodecylamine oxide, dipropyltetradecylamine oxide, methylethylhexadecylamine oxide, dodecylamidopropyl dimethylamine oxide, cetyl dimethylamine oxide, stearyl dimethylamine oxide, tallow dimethylamine oxide and dimethyl-2-hydroxyoctadecylamine oxide. Preferred are C10-C18 alkyl dimethylamine oxide, and C10-18 acylamido alkyl dimethylamine oxide.
Surfactants may be present in amounts from 0 to 10% by weight, preferably from 0.1% to 10%, and most preferably from 0.25% to 6% by weight of the total composition.
Builders for use herein include phosphate builders and non-phosphate builders, preferably the builder is a non-phosphate builder. If present, builders are used in a level of from 5 to 60%, preferably from 10 to 50% by weight of the composition. In some embodiments the product comprises a mixture of phosphate and non-phosphate builders.
Preferred phosphate builders include mono-phosphates, di-phosphates, tri-polyphosphates or oligomeric-poylphosphates. The alkali metal salts of these compounds are preferred, in particular the sodium salts. An especially preferred builder is sodium tripolyphosphate (STPP).
In addition to the aminocarboxylic builders in the particle of the invention, the composition can comprise carbonate and/or citrate.
The particle of the invention is present in the composition in an amount of at least 1%, more preferably at least 5%, even more preferably at least 10%, and most especially at least 20% by weight of the total composition.
Preferably builders are present in an amount of up to 50%, more preferably up to 45%, even more preferably up to 40%, and especially up to 35% by weight of the composition. In preferred embodiments the composition contains 20% by weight of the composition or less of phosphate builders, more preferably 10% by weight of the composition or less, most preferably they are substantially free of phosphate builders.
Other non-phosphate builders include homopolymers and copolymers of polycarboxylic acids and their partially or completely neutralized salts, monomeric polycarboxylic acids and hydroxycarboxylic acids and their salts. Preferred salts of the abovementioned compounds are the ammonium and/or alkali metal salts, i.e. the lithium, sodium, and potassium salts, and particularly preferred salts are the sodium salts.
Suitable polycarboxylic acids are acyclic, alicyclic, heterocyclic and aromatic carboxylic acids, in which case they contain at least two carboxyl groups which are in each case separated from one another by, preferably, no more than two carbon atoms. Polycarboxylates which comprise two carboxyl groups include, for example, water-soluble salts of, malonic acid, (ethyl enedioxy) diacetic acid, maleic acid, diglycolic acid, tartaric acid, tartronic acid and fumaric acid. Polycarboxylates which contain three carboxyl groups include, for example, water-soluble citrate. Correspondingly, a suitable hydroxycarboxylic acid is, for example, citric acid. Another suitable polycarboxylic acid is the homopolymer of acrylic acid. Other suitable builders are disclosed in WO 95/01416, to the contents of which express reference is hereby made.
The polymer, if present, is used in any suitable amount from about 0.1% to about 50%, preferably from 0.5% to about 20%, more preferably from 1% to 10% by weight of the composition. Sulfonated/carboxylated polymers are particularly suitable for the composition of the invention.
Suitable sulfonated/carboxylated polymers described herein may have a weight average molecular weight of less than or equal to about 100,000 Da, or less than or equal to about 75,000 Da, or less than or equal to about 50,000 Da, or from about 3,000 Da to about 50,000, preferably from about 5,000 Da to about 45,000 Da.
As noted herein, the sulfonated/carboxylated polymers may comprise (a) at least one structural unit derived from at least one carboxylic acid monomer having the general formula (I):
Preferred carboxylic acid monomers include one or more of the following: acrylic acid, maleic acid, itaconic acid, methacrylic acid, or ethoxylate esters of acrylic acids, acrylic and methacrylic acids being more preferred. Preferred sulfonated monomers include one or more of the following: sodium (meth)allyl sulfonate, vinyl sulfonate, sodium phenyl (meth)allyl ether sulfonate, or 2-acrylamido-methyl propane sulfonic acid. Preferred non-ionic monomers include one or more of the following: methyl (meth)acrylate, ethyl (meth)acrylate, t-butyl (meth)acrylate, methyl (meth)acrylamide, ethyl (meth)acrylamide, t-butyl (meth)acrylamide, styrene, or α-methyl styrene.
Preferably, the polymer comprises the following levels of monomers: from about 40 to about 90%, preferably from about 60 to about 90% by weight of the polymer of one or more carboxylic acid monomer; from about 5 to about 50%, preferably from about 10 to about 40% by weight of the polymer of one or more sulfonic acid monomer; and optionally from about 1% to about 30%, preferably from about 2 to about 20% by weight of the polymer of one or more non-ionic monomer. An especially preferred polymer comprises about 70% to about 80% by weight of the polymer of at least one carboxylic acid monomer and from about 20% to about 30% by weight of the polymer of at least one sulfonic acid monomer.
The carboxylic acid is preferably (meth)acrylic acid. The sulfonic acid monomer is preferably one of the following: 2-acrylamido methyl-1-propanesulfonic acid, 2-methacrylamido-2-methyl-1-propanesulfonic acid, 3-methacrylamido-2-hydroxypropanesulfonic acid, allysulfonic acid, methallysulfonic acid, allyloxybenzenesulfonic acid, methallyloxybenzensulfonic acid, 2-hydroxy-3-(2-propenyloxy)propanesulfonic acid, 2-methyl-2-propene-1-sulfonic acid, styrene sulfonic acid, vinylsulfonic acid, 3-sulfopropyl acrylate, 3-sulfopropyl methacrylate, sulfomethylacrylamid, sulfomethylmethacrylamide, and water soluble salts thereof. The unsaturated sulfonic acid monomer is most preferably 2-acrylamido-2-propanesulfonic acid (AMPS).
Preferred commercial available polymers include: Alcosperse 240, Aquatreat AR 540 and Aquatreat MPS supplied by Alco Chemical; Acumer 3100, Acumer 2000, Acusol 587G and Acusol 588G supplied by Rohm & Haas; Goodrich K-798, K-775 and K-797 supplied by BF Goodrich; and ACP 1042 supplied by ISP technologies Inc. Particularly preferred polymers are Acusol 587G and Acusol 588G supplied by Rohm & Haas.
Other suitable organic polymer for use herein includes a polymer comprising an acrylic acid backbone and alkoxylated side chains, said polymer having a molecular weight of from about 2,000 to about 20,000, and said polymer having from about 20 wt % to about 50 wt % of an alkylene oxide. The polymer should have a molecular weight of from about 2,000 to about 20,000, or from about 3,000 to about 15,000, or from about 5,000 to about 13,000. The alkylene oxide (AO) component of the polymer is generally propylene oxide (PO) or ethylene oxide (EO) and generally comprises from about 20 wt % to about 50 wt %, or from about 30 wt % to about 45 wt %, or from about 30 wt % to about 40 wt % of the polymer. The alkoxylated side chains of the water soluble polymers may comprise from about 10 to about 55 AO units, or from about 20 to about 50 AO units, or from about 25 to 50 AO units. The polymers, preferably water soluble, may be configured as random, block, graft, or other known configurations. Methods for forming alkoxylated acrylic acid polymers are disclosed in U.S. Pat. No. 3,880,765.
Other suitable organic polymer for use herein includes polyaspartic acid (PAS) derivatives as described in WO 2009/095645 A1.
According to this nomenclature, for instance the substitution of glutamic acid for glycine in position 195 is shown as G195E. A deletion of glycine in the same position is shown as G195*, and insertion of an additional amino acid residue such as lysine is shown as G195GK. Where a specific enzyme contains a “deletion” in comparison with other enzyme and an insertion is made in such a position this is indicated as *36D for insertion of an aspartic acid in position 36. Multiple mutations are separated by pluses, i.e.: S99G+V102N, representing mutations in positions 99 and 102 substituting serine and valine for glycine and asparagine, respectively. Where the amino acid in a position (e.g. 102) may be substituted by another amino acid selected from a group of amino acids, e.g. the group consisting of N and I, this will be indicated by V102N/I.
In all cases, the accepted IUPAC single letter or triple letter amino acid abbreviation is employed.
The numbering used herein is numbering versus the so-called BPN' numbering scheme which is commonly used in the art and is illustrated for example in WO00/37627.
The relatedness between two amino acid sequences is described by the parameter “identity”. For purposes of the present invention, the alignment of two amino acid sequences is determined by using the Needle program from the EMBOSS package (http://emboss.org) version 2.8.0. The Needle program implements the global alignment algorithm described in Needleman, S. B. and Wunsch, C. D. (1970) J. Mol. Biol. 48, 443-453. The substitution matrix used is BLOSUM62, gap opening penalty is 10, and gap extension penalty is 0.5.
The degree of identity between an amino acid sequence of and enzyme used herein (“invention sequence”) and a different amino acid sequence (“foreign sequence”) is calculated as the number of exact matches in an alignment of the two sequences, divided by the length of the “invention sequence” or the length of the “foreign sequence”, whichever is the shortest. The result is expressed in percent identity. An exact match occurs when the “invention sequence” and the “foreign sequence” have identical amino acid residues in the same positions of the overlap. The length of a sequence is the number of amino acid residues in the sequence.
Preferred enzyme for use herein includes a protease. Suitable proteases include metalloproteases and serine proteases, including neutral or alkaline microbial serine proteases, such as subtilisins (EC 3.4.21.62). Suitable proteases include those of animal, vegetable or microbial origin. In one aspect, such suitable protease may be of microbial origin. The suitable proteases include chemically or genetically modified mutants of the aforementioned suitable proteases. In one aspect, the suitable protease may be a serine protease, such as an alkaline microbial protease or/and a trypsin-type protease. Examples of suitable neutral or alkaline proteases include:
Suitable commercially available protease enzymes include those sold under the trade names Alcalase®, Savinase®, Primase®, Durazym®, Polarzyme®, Kannase®, Liquanase®, Ovozyme®, Neutrase®, Everlase® and Esperase® by Novozymes A/S (Denmark), those sold under the tradename Maxatase®, Maxacal®, Maxapem®, Properase®, Purafect®, Purafect Prime®, Purafect Ox®, FN3®, FN4®, Excellase® and Purafect OXP® by Genencor International, those sold under the tradename Opticlean® and Optimase® by Solvay Enzymes, those available from Henkel/Kemira, namely BLAP (sequence shown in FIG. 29 of U.S. Pat. No. 5,352,604 with the following mutations S99D+S101 R+S103A+V104I+G159S, hereinafter referred to as BLAP), BLAP R (BLAP with S3T+V4I+V199M+V205I+L217D), BLAP X (BLAP with S3T+V4I+V205I) and BLAP F49 (BLAP with S3T+V4I+A194P+V199M+V205I+L217D)—all from Henkel/Kemira; and KAP (Bacillus alkalophilus subtilisin with mutations A230V+S256G+S259N) from Kao. Preferred for use herein in terms of performance is a dual protease system, in particular a system comprising a protease comprising S99SD+S99A mutations (BPN' numbering system) versus either the PB92 wild-type (SEQ ID NO:2 in WO 08/010925) or the subtilisin 309 wild-type (sequence as per PB92 backbone, except comprising a natural variation of N87S). and a DSM14391 Bacillus Gibsonii enzyme, as described in WO 2009/021867 A2.
Preferred levels of protease in the product of the invention include from about 0.1 to about 10, more preferably from about 0.5 to about 5 and especially from about 1 to about 4 mg of active protease per grams of product.
(c) variants exhibiting at least 90% identity with SEQ ID No. 4 in WO06/002643, the wild-type enzyme from Bacillus SP722, especially variants with deletions in the 183 and 184 positions and variants described in WO 00/60060, which is incorporated herein by reference.
(d) variants exhibiting at least 95% identity with the wild-type enzyme from Bacillus sp.707 (SEQ ID NO:7 in U.S. Pat. No. 6,093, 562), especially those comprising one or more of the following mutations M202, M208, S255, R172, and/or M261. Preferably said amylase comprises one or more of M202L, M202V, M202S, M202T, M202I, M202Q, M202W, S255N and/or R172Q. Particularly preferred are those comprising the M202L or M202T mutations.
Preferred -amylases include the below variants of SEQ ID No. 12 in WO 06/002643:
Preferred amylases include those comprising the following sets of mutations:
Suitable commercially available alpha-amylases include DURAMYL®, LIQUEZYME®, TERMAMYL®, TERMAMYL ULTRA®, NATALASE®, SUPRAMYL®, STAINZYME®, STAINZYME PLUS®, POWERASE®, FUNGAMYL® and BAN® (Novozymes A/S, Bagsvaerd, Denmark), KEMZYM® AT 9000 Biozym Biotech Trading GmbH Wehlistrasse 27b A-1200 Wien Austria, RAPIDASE®, PURASTAR®, ENZYSIZE®, OPTISIZE HT PLUS® and PURASTAR OXAM® (Genencor International Inc., Palo Alto, Calif.) and KAM® (Kao, 14-10 Nihonbashi Kayabacho, 1-chome, Chuo-ku Tokyo 103-8210, Japan). Amylases especially preferred for use herein include NATALASE®, STAINZYME®, STAINZYME PLUS®, POWERASE® and mixtures thereof.
Additional enzymes suitable for use in the product of the invention can comprise one or more enzymes selected from the group comprising hemicellulases, cellulases, cellobiose dehydrogenases, peroxidases, proteases, xylanases, lipases, phospholipases, esterases, cutinases, pectinases, mannanases, pectate lyases, keratinases, reductases, oxidases, phenoloxidases, lipoxygenases, ligninases, pullulanases, tannases, pentosanases, malanases, β-glucanases, arabinosidases, hyaluronidase, chondroitinase, laccase, amylases, and mixtures thereof.
The product of the invention preferably comprises other enzymes in addition to the protease and/or amylase. Cellulase enzymes are preferred additional enzymes, particularly microbial-derived endoglucanases exhibiting endo-beta-1,4-glucanase activity (E.C. 3.2.1.4), including a bacterial polypeptide endogenous to a member of the genus Bacillus which has a sequence of at least 90%, preferably 94%, more preferably 97% and even more preferably 99% identity to the amino acid sequence SEQ ID NO:2 in U.S. Pat. No. 7,141,403B2 and mixtures thereof. Preferred commercially available cellulases for use herein are Celluzyme®, Celluclean®, Whitezyme® (Novozymes A/S) and Puradax HA® and Puradax® (Genencor International).
Preferably, the product of the invention comprises at least 0.01 mg of active amylase per gram of composition, preferably from about 0.05 to about 10, more preferably from about 0.1 to about 6, especially from about 0.2 to about 4 mg of amylase per gram of composition.
Preferably, the protease and/or amylase of the product of the invention are in the form of granulates, the granulates comprise less than 29% of efflorescent material by weight of the granulate or the efflorescent material and the active enzyme (protease and/or amylase) are in a weight ratio of less than 4:1.
Preferred drying aids for use herein include polyesters, especially anionic polyesters formed from monomers of terephthalic acid, 5-sulphoisophthalic acid, alkyl diols or polyalkylene glycols, and, polyalkyleneglycol monoalkylethers. Suitable polyesters to use as drying aids are disclosed in WO 2008/110816. Other suitable drying aids include specific polycarbonate-, polyurethane- and/or polyurea-polyorganosiloxane compounds or precursor compounds thereof of the reactive cyclic carbonate and urea type, as described in WO 2008/119834.
Improved drying can also be achieved by a process involving the delivery of surfactant and an anionic polymer as proposed in WO 2009/033830 or by combining a specific non-ionic surfactant in combination with a sulfonated polymer as proposed in WO 2009/033972.
Preferably the composition of the invention comprises from 0.1% to 10%, more preferably from 0.5 to 5% and especially from 1% to 4% by weight of the composition of a drying aid.
Preferred silicates are sodium silicates such as sodium disilicate, sodium metasilicate and crystalline phyllosilicates. Silicates if present are at a level of from about 1 to about 20%, preferably from about 5 to about 15% by weight of composition.
Inorganic and organic bleaches are suitable cleaning actives for use herein. Inorganic bleaches include perhydrate salts such as perborate, percarbonate, perphosphate, persulfate and persilicate salts. The inorganic perhydrate salts are normally the alkali metal salts. The inorganic perhydrate salt may be included as the crystalline solid without additional protection. Alternatively, the salt can be coated.
Alkali metal percarbonates, particularly sodium percarbonate are preferred perhydrates for use herein. The percarbonate is most preferably incorporated into the products in a coated form which provides in-product stability.
Potassium peroxymonopersulfate is another inorganic perhydrate salt of utility herein.
Typical organic bleaches are organic peroxyacids including diacyl and tetraacylperoxides, especially diperoxydodecanedioc acid, diperoxytetradecanedioc acid, and diperoxyhexadecanedioc acid. Dibenzoyl peroxide is a preferred organic peroxyacid herein. Mono- and diperazelaic acid, mono- and diperbrassylic acid, and Nphthaloylaminoperoxicaproic acid are also suitable herein.
Further typical organic bleaches include the peroxy acids, particular examples being the alkylperoxy acids and the arylperoxy acids. Preferred representatives are (a) peroxybenzoic acid and its ring-substituted derivatives, such as alkylperoxybenzoic acids, but also peroxy-α-naphthoic acid and magnesium monoperphthalate, (b) the aliphatic or substituted aliphatic peroxy acids, such as peroxylauric acid, peroxystearic acid, ε-phthalimidoperoxycaproic acid{phthaloiminoperoxyhexanoic acid (PAP)}, o-carboxybenzamidoperoxycaproic acid, N-nonenylamidoperadipic acid and N-nonenylamidopersuccinates, and (c) aliphatic and araliphatic peroxydicarboxylic acids, such as 1,12-diperoxycarboxylic acid, 1,9-diperoxyazelaic acid, diperoxysebacic acid, diperoxybrassylic acid, the diperoxyphthalic acids, 2-decyldiperoxybutane-1,4-dioic acid, N,N-terephthaloyldi(6-aminopercaproic acid).
Bleach activators are typically organic peracid precursors that enhance the bleaching action in the course of cleaning at temperatures of 60° C. and below. Bleach activators suitable for use herein include compounds which, under perhydrolysis conditions, give aliphatic peroxoycarboxylic acids having preferably from 1 to 10 carbon atoms, in particular from 2 to 4 carbon atoms, and/or optionally substituted perbenzoic acid. Suitable substances bear O-acyl and/or N-acyl groups of the number of carbon atoms specified and/or optionally substituted benzoyl groups. Preference is given to polyacylated alkylenediamines, in particular tetraacetylethylenediamine (TAED), acylated triazine derivatives, in particular 1,5-diacetyl-2,4-dioxohexahydro-1,3,5-triazine (DADHT), acylated glycolurils, in particular tetraacetylglycoluril (TAGU), N-acylimides, in particular N-nonanoylsuccinimide (NOSI), acylated phenolsulfonates, in particular n-nonanoyl- or isononanoyloxybenzenesulfonate (n- or iso-NOBS), carboxylic anhydrides, in particular phthalic anhydride, acylated polyhydric alcohols, in particular triacetin, ethylene glycol diacetate and 2,5-diacetoxy-2,5-dihydrofuran and also triethylacetyl citrate (TEAC). Bleach activators if included in the compositions of the invention are in a level of from about 0.1 to about 10%, preferably from about 0.5 to about 2% by weight of the total composition.
Bleach catalysts preferred for use herein include the manganese triazacyclononane and related complexes (U.S. Pat. No. 4,246,612, U.S. Pat. No. 5,227,084); Co, Cu, Mn and Fe bispyridylamine and related complexes (U.S. Pat. No. 5,114,611); and pentamine acetate cobalt(III) and related complexes(U.S. Pat. No. 4,810,410). A complete description of bleach catalysts suitable for use herein can be found in WO 99/06521, pages 34, line 26 to page 40, line 16. Bleach catalyst if included in the compositions of the invention are in a level of from about 0.1 to about 10%, preferably from about 0.5 to about 2% by weight of the total composition.
Metal care agents may prevent or reduce the tarnishing, corrosion or oxidation of metals, including aluminium, stainless steel and non-ferrous metals, such as silver and copper. Preferably the composition of the invention comprises from 0.1 to 5%, more preferably from 0.2 to 4% and specially from 0.3 to 3% by weight of the composition of a metal care agent, preferably the metal care agent is a zinc salt.
The dimensions and values disclosed herein are not to be understood as being strictly limited to the exact numerical values recited. Instead, unless otherwise specified, each such dimension is intended to mean both the recited value and a functionally equivalent range surrounding that value. For example, a dimension disclosed as “40 mm” is intended to mean “about 40 mm”
Particles according to the invention are made according to the following process. 1000 g of Trilon M liquid (MGDA tri-sodium salt, approximately 40% active, supplied by BASF) is mixed with 15 g of concentrated (98%) sulphuric acid to achieve a pH approximately 10.7. The resulting solution is then heated to 60° C. with agitation and spray dried in an APB lab scale spray drier at a rate of 7.5 l/hour through two fluid nozzles using atomized air at 2 bars. The inlet drying air is at a temperature between 265°-300° C. The air outlet temperature is between 70°-80° C.
The resulting intermediate particles are then compacted to form 10 g tablets in a 1.25 inch circular dye using a total force of 10 tons. The resulting tablets are ground in a coffee grinder and sieved between 250 μm and 1700 μm and then subsequently dried further in an oven at 100° C. They are then coated with 25% sodium sulphate solution by weight of the solution, using an air atomised nozzle to spray the solution onto the particles in a well-fluidized bed with an air inlet temperature of 150° C. to give the final particles. The particles exhibit high resistance to moisture and have good flowability and solubility.
Every document cited herein, including any cross referenced or related patent or application, is hereby incorporated herein by reference in its entirety unless expressly excluded or otherwise limited. The citation of any document is not an admission that it is prior art with respect to any invention disclosed or claimed herein or that it alone, or in any combination with any other reference or references, teaches, suggests or discloses any such invention. Further, to the extent that any meaning or definition of a term in this document conflicts with any meaning or definition of the same term in a document incorporated by reference, the meaning or definition assigned to that term in this document shall govern.
While particular embodiments of the present invention have been illustrated and described, it would be obvious to those skilled in the art that various other changes and modifications can be made without departing from the spirit and scope of the invention. It is therefore intended to cover in the appended claims all such changes and modifications that are within the scope of this invention.
Number | Date | Country | Kind |
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11185850.2 | Oct 2011 | EP | regional |